1,1,1,3,3-Pentachloropropane (240 fa) from Vinyl chloride monomer and carbon chloride from vinyl chloride monomer and carbon chloride ; single route, at producer ; 216.3 g/mol | EU-28 | agg | Sphera |
1,1,1,3,3-Pentachloropropane (240 fa) from Vinyl chloride monomer and carbon chloride from vinyl chloride monomer and carbon chloride ; single route, at producer ; 216.3 g/mol | DE | agg | Sphera |
1,1,1,3,3-Pentafluoropropane (245 fa) from Vinyl chloride monomer and carbon chloride via 240fa from Vinyl chloride monomer and carbon chloride via 240fa and hydrogen fluoride ; single route, at producer ; 1404.1 kg/m3, 134.05 g/mol | DE | agg | Sphera |
1,1,1,3,3-Pentafluoropropane (245 fa) from Vinyl chloride monomer and carbon chloride via 240fa from Vinyl chloride monomer and carbon chloride via 240fa ; single route, at producer ; 1404.1 kg/m3, 134.05 g/mol | EU-28 | agg | Sphera |
1,1,1-Trichloroethane (methylchloroform) chlorination of ethane ; production mix, at plant ; 1.34 g/cm3, 133.42 g/mol | DE | agg | Sphera |
1,12-Dodecandioic acid (from Cyclododecatriene) hydrogenation of cyclododecatriene, oxidation of cyclodocecane ; single route, at plant ; 1.15 g/cm3, 230.31 g/mol | DE | agg | Sphera |
1,1-Difluoroethane (HFC 152a) hydrofluorination of vinyl chloride ; single producer, at plant ; 3.04 kg/m3 at 0°C, 66.05 g/mol | DE | agg | Sphera |
1,3-bis[3-(dimethylamino)propyl]urea reaction of urea with N,N-dimethylamino-propylamine ; single route, at plant ; 230.35 g/mol | EU-28 | agg | Sphera |
1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | NL | agg | Sphera |
1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | CN | agg | Sphera |
1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | ES | agg | Sphera |
1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | JP | agg | Sphera |
1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | NO | agg | Sphera |
1,4-Dioxane (Diethylene oxide) dehydration and ring closure of diethylene glycol ; production mix, at plant ; 1.03 g/cm3, 88.11 g/mol | DE | agg | Sphera |
1,6-Hexanediol (approximation) catalytic hydrogenation of adipic acid ; production mix, at plant ; 118.18 g/mol | EU-28 | agg | Sphera |
1,6-Hexanediol (approximation) catalytic hydrogenation of adipic acid ; single producer, at plant ; 118.18 g/mol | DE | agg | Sphera |
1-Aminoanthraquinone from chlorobenzoic acid and xylene ; production mix, at plant ; 223.23 g/mol | US | agg | Sphera |
1-Decanol (approximation) Hydrogenation of decanoic acid, based on palm kernel oil ; production mix, at plant ; 0.8297 g/cm3, 158.28 g/mol | EU-28 | agg | Sphera |
1-Decene by-product Linear Alphaolefine (LAO) (mass allocation) (approximation) oligomerization of ethylene, by-product Linear Alphaolefine ; single route, at plant ; 0.74 g/cm3, 140.27 g/mol | DE | agg | Sphera |
1-Dodecanol hydrogenation of dodecanoic acid ; production mix, at plant ; 0.83 g/cm3, 186.34 g/mol | EU-28 | agg | Sphera |
1-Dodecanol hydrogenation of dodecanoic acid ; production mix, at plant ; 0.83 g/cm3, 186.34 g/mol | DE | agg | Sphera |
1-Tetradecanoic acid (Myristic acid) (mass allocation) Enzymatric cleavage of palm oil ; single route, at producer ; 0.86 g/cm3, 228.38 g/mol | DE | agg | Sphera |
2-(Perfluorohexyl)ethyl iodide radical-catalysed addition of ethylene to perfluorohexyl iodide ; single route, at producer ; 474 g/mol | US | agg | Sphera |
2-(Perfluorohexyl)ethyl iodide radical-catalysed addition of ethylene to perfluorohexyl iodide ; single route, at producer ; 474 g/mol | DE | agg | Sphera |
2,4-Dimethylbenzaldehyde reaction of xylene with carbon monoxide ; single producer, at plant ; density 0.962 g/mL at 25 °C, molar mass 134 g... | DE | agg | Sphera |
2,4-Dimethylbenzaldehyde reaction of xylene with carbon monoxide ; single producer, at plant ; density 0.962 g/mL at 25 °C, molar mass 134 g... | EU-28 | agg | Sphera |
2-Acrylamido-2-methylpropane sulfonic acid (AMPS) Ritter reaction of acrylonitrile and isobutylene in the presence of sulfuric acid and water ; single route, at producer ; 1.1 g/cm3, 207,24 g/mol | EU-28 | agg | Sphera |
2-Dimethylaminoethanol (DMAE) reaction of dimethylamine and ethylene oxide ; production mix, at plant ; 0.89 g/cm3, 89.14 g/mol | EU-28 | agg | Sphera |
2-Ethylhexanol from propylene Aldolization of butyraldehyde ; production mix, at plant ; 0.83 g/cm3, 130.23 g/mol | DE | agg | Sphera |
2-Ethylhexanol from propylene Aldolization of butyraldehyde ; production mix, at plant ; 0.83 g/cm3, 130.23 g/mol | US | agg | Sphera |
2-Ethylhexanol from propylene Aldolization of butyraldehyde ; production mix, at plant ; 0.83 g/cm3, 130.23 g/mol | EU-28 | agg | Sphera |
2-Etylhexaltallowat Transesterification ; production mix, at plant ; estimation | DE | agg | Sphera |
2K-dispersion adhesive mixing polyurethane, methyl ethyl ketone, water and hardener ; production mix, at plant ; contains 5% hardener | DE | agg | Sphera |
2-keto-L-gulonic acid butyl ester esterification of 2-keto-L-gulonic acid with butanol ; production mix, at plant ; 250 g/mol | US | agg | Sphera |
2-keto-L-gulonic acid butyl ester (97%) esterification of 2-keto-L-gulonic acid with butanol ; production mix, at plant ; 97% concentrated | US | agg | Sphera |
2-keto-L-gulonic acid preparation bacteria cultivation, fermentation of L- sorbose ; production mix, at plant ; 194.14 g/mol | US | agg | Sphera |
2-methyl-1,3-propanediol from propylene oxide ; single route, at plant ; 1.02 g/cm3, 90.12 g/mol, 25.5 MJ/kg | EU-28 | agg | Sphera |
2-Octanol by-product sebacic acid - average, 50:50 mix of best case and worst case scenario technology mix, saponification of castor oil with alkali ; production mix, at producer ; 0.819 g/mL at 25 °C, 130.23 g/mol | CN | agg | Sphera |
3-Aminopropyltriethoxysilane (approximation) reaction of chloroalkylsilane with ammonia or an organic amino compound ; production mix, at plant ; 0.946 g/cm3, 221.37 g/mol | DE | agg | Sphera |
3-Aminopropyltriethoxysilane (approximation) reaction of chloroalkylsilane with ammonia or an organic amino compound ; production mix, at plant ; 0.946 g/cm3, 221.37 g/mol | EU-28 | agg | Sphera |
3-Glycidyloxypropyltrimethoxysilane (GLYMO) (approximation) Heterogeneous platinum-catalyzed hydrosilylation by reacting Allyl glycidyl ether with Trimethoxysilane ; single route, at producer ; 236.34 g/mol | EU-28 | agg | Sphera |
3-Hydroxy-2-Naphthoic acid carboxylation of potassium naphtholate ; production mix, at plant ; 188.18 g/mol | DE | agg | Sphera |
3-Mercaptopropionic acid (approximation) reaction of methanthiol (or H2S) with acrylic acid ; single route, at plant ; 1.218 g/mL at 25 °C, molar mass 106.14 g/mol | EU-28 | agg | Sphera |
4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (approximation) sulfonation of chlorobenzene ; production mix, at plant ; 287 g/mol | US | agg | Sphera |
4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (approximation) sulfonation of chlorobenzene ; production mix, at plant ; 287 g/mol | DE | agg | Sphera |
4-Hydroxy 4-methyl-2-pentanone ketone condensation ; single producer, at plant ; density 0.931 g/mL at 25 °C, molar mass 116.1... | DE | agg | Sphera |
6-Hydroxy-2-Naphthoic acid carboxylation of potassium naphtholate ; production mix, at plant ; 188.18 g/mol | US | agg | Sphera |
6-Hydroxy-2-Naphthoic acid carboxylation of potassium naphtholate ; production mix, at plant ; 188.18 g/mol | DE | agg | Sphera |
ABS GF 30 injection moulding of acrylonitrile butadiene styrene with glass fibres ; production mix, at plant ; 30% glass fibres | DE | agg | Sphera |
Acetic acid (60%) from methanol (low pressure carbonylation) (Monsanto process) catalytic reaction of methanol and carbon monoxide ; single route, at plant ; 1.05 g/cm3, 605 g/mol | DE | agg | Sphera |
Acetic acid by-product Polyvinyl Alcohol (PVAL) from vinyl acetate hydrolysis of vinyl acetate ; single route, at plant ; 1.049 g/cm3, 60.05 g/mol, 12.1 MJ/kg net calorif... | DE | agg | Sphera |
Acetic acid from methanol (coal based MeOH + Syngas) (low pressure carbonylation) (Monsanto process) catalytic reaction of methanol and carbon monoxide ; single route, at plant ; 1.05 g/cm3, 605 g/mol | CN | agg | Sphera |
Acetic acid from methanol (low pressure carbonylation) (Monsanto process) catalytic reaction of methanol and carbon monoxide ; single route, at plant ; 1.05 g/cm3, 605 g/mol | CN | agg | Sphera |
Acetic acid from methanol (low pressure carbonylation) (Monsanto process) catalytic reaction of methanol and carbon monoxide ; single route, at plant ; 1.05 g/cm3, 605 g/mol | EU-28 | agg | Sphera |
Acetic acid from methanol (low pressure carbonylation) (Monsanto process) catalytic reaction of methanol and carbon monoxide ; single route, at plant ; 1.05 g/cm3, 605 g/mol | MY | agg | Sphera |
Acetic anhydride via multi-stage process ; production mix, at plant ; 1.08 g/cm3, 102.09 g/mol | DE | agg | Sphera |
Acetic anhydride via multi-stage process ; production mix, at plant ; 1.08 g/cm3, 102.09 g/mol | EU-28 | agg | Sphera |
Acetic anhydride via multi-stage process ; production mix, at plant ; 1.08 g/cm3, 102.09 g/mol | CN | agg | Sphera |
Acetic anhydride (coal based energy + feedstock) via multi-stage process ; production mix, at plant ; 1.08 g/cm3, 102.09 g/mol | CN | agg | Sphera |
Acetoncyanhydrine (ACH) with HCN from acrylonitrile by-product with HCN from acrylonitrile by-product ; production mix, at plant ; 0.93 g/cm3, 85.11 g/mol | DE | agg | Sphera |
Acetone by-product phenol, methyl styrene (from Cumene) Hock Process, oxidation of cumene ; single route, at plant ; 0.79 g/cm3, 58 g/mol | CN | agg | Sphera |
Acetone by-product phenol, methyl styrene (from Cumene) Hock Process, oxidation of cumene ; single route, at plant ; 0.79 g/cm3, 58 g/mol | JP | agg | Sphera |
Acetone by-product phenol, methyl styrene (from Cumene) Hock Process, oxidation of cumene ; single route, at plant ; 0.79 g/cm3, 58 g/mol | TH | agg | Sphera |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product ; production mix, at plant ; 0.93 g/cm3, 85.11 g/mol | IT | agg | Sphera |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product ; production mix, at plant ; 0.93 g/cm3, 85.11 g/mol | DE | agg | Sphera |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product ; production mix, at plant ; 0.93 g/cm3, 85.11 g/mol | EU-28 | agg | Sphera |
Acetonitrile ammoxidation of propene ; production mix, at plant ; 786 mg/mL, 41 g/mol | GB | agg | Sphera |
Acetonitrile (Recovery in acrylonitrile production) ammoxidation of propene ; single route, at plant ; 0.786 g/cm3, 41.05 g/mol | DE | agg | Sphera |
Acetophenone (by-product of main products acetone and phenol via cumene) by-product of Hock Process, oxidation of cumene ; single route, at plant ; 1.07 g/cm3, 94 g/mol | DE | agg | Sphera |
Acetophenone (by-product of main products acetone and phenol via cumene) by-product of Hock Process, oxidation of cumene ; single route, at plant ; 1.07 g/cm3, 94 g/mol | EU-28 | agg | Sphera |
Acrylamide (catalytic hydrolysis) (50% solution) catalytic hydration of acrylonitrile ; single producer, at plant ; 1.13 g/cm3, 71.08 g/mol | DE | agg | Sphera |
Acrylamide (enzymatic hydration) (50% solution) enzymatic hydration of acrylonitrile ; single route, at plant ; 1.13 g/cm3, 71.08 g/mol | DE | agg | Sphera |
Acrylamide (enzymatic hydration) (50% solution) enzymatic hydration of acrylonitrile ; single route, at plant ; 1.13 g/cm3, 71.08 g/mol | CN | agg | Sphera |
Acrylate (emulsion) emulsion polymerization ; single route, at plant ; 44% solid content | EU-28 | agg | Sphera |
Acrylate (emulsion) emulsion polymerization ; single producer, at plant ; 44% solid content | DE | agg | Sphera |
Acrylate resin (epoxy functional) polymerisation ; single route, at plant ; 30.000- 100.000 g/mol | EU-28 | agg | Sphera |
Acrylate resin (epoxy-functional) polymerisation ; single route, at plant ; 30.000- 100.000 g/mol | DE | agg | Sphera |
Acrylate resin (solvent-systems) polymerisation ; single route, at plant ; 30.000- 100.000 g/mol | DE | agg | Sphera |
Acrylcopolymer - 100% MMA bulk polymerisation, from methyl methacrylate ; production mix, at plant ; 1.18 g/cm3, 24 MJ net calorific value.. | DE | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | BE | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | NL | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | TH | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | CN | agg | Sphera |
Acrylonitrile (AN) propene ammoxidation, by- product ammonium sulphate ; production mix, at plant ; 0.81 g/cm3, 53.06 g/mol | BE | agg | Sphera |
Acrylonitrile (AN) by-product ammonium sulphate, hydrogen cyanide propene ammoxidation, by- product ammonium sulphate ; production mix, at plant ; 0.81 g/cm3, 53.06 g/mol | JP | agg | Sphera |
Acrylonitrile-Butadiene-Styrene Granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene ; production mix, at plant ; 1.060- 1.080 g/cm3, 39.0 MJ/kg net calorific v... | NL | agg | Sphera |
Acrylonitrile-Butadiene-Styrene Granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene ; production mix, at plant ; 1.060- 1.080 g/cm3, 39.0 MJ/kg net calorific v... | BE | agg | Sphera |
Acrylonitrile-butadiene-styrene-granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene ; production mix, at plant ; 1.060- 1.080 g/cm3, 39.0 MJ/kg net calorific v... | CN | agg | Sphera |
Activated carbon technology mix ; production mix, at plant ; porous carbon structure, 35.2 MJ/kg net calori... | JP | agg | Sphera |
Activated carbon technology mix ; production mix, at plant ; porous carbon structure, 35.2 MJ/kg net calori... | CN | agg | Sphera |
Activated carbon technology mix ; production mix, at plant ; porous carbon structure, 35.2 MJ/kg net calori... | EU-28 | agg | Sphera |
Adhesive system MDF (35% H2O content) hydromethylation and condensation reactions of melamine, urea and formaldehyde ; production mix, at plant ; 35% H2O content | DE | agg | Sphera |
Adhesive system MUF (35%M i.T., 35% H2O content) hydromethylation and condensation reactions of melamine, urea and formaldehyde ; production mix, at plant ; 35% M i.T., 35% H2O | DE | agg | Sphera |
Adhesive system mUF (36% moisture) hydromethylation and condensation reactions of urea and formaldehyde ; production mix, at plant ; 36% moisture | DE | agg | Sphera |
Adhesive system MUPF (35% H2O content) hydromethylation and condensation reactions of melamine, urea, phenol and formaldehyde ; single route, at plant ; 35% H2O | DE | agg | Sphera |
Adhesive system PF (F/P=1.8; 40% H2O content) Phenol- formaldehyde condensation in caustic solution ; single producer, at plant ; F/P=1.8; 40% H2O | DE | agg | Sphera |
Adhesive system PF (F/P=1.8; 52% H2O content) Phenol- formaldehyde condensation in caustic solution ; single producer, at plant ; F/P=1,8; 52% H2O | DE | agg | Sphera |
Adhesive system polyurethane-prepolymer reaction of methylene diisocyanate and polyether polyol ; production mix, at plant ; 50% methylene diisocyanate, 50% polyether poly... | DE | agg | Sphera |
Adhesive system UFm (4% Melamin; 35% H2O content) hydromethylation and condensation reactions of urea, melamin and formaldehyde ; single route, at plant ; 4% Melamin; 35% H2O | DE | agg | Sphera |
Adhesive system Urea Formaldehyde (UF) (35% H2O content) hydromethylation and condensation reactions of urea and formaldehyde ; single producer, at plant ; 35% H2O | DE | agg | Sphera |
Adipic acid from cyclohexane purified, cyclohexane oxidation route, with nitric acid ; production mix, at plant ; 1.36 g/cm3, 146 g/mol | EU-28 | agg | Sphera |
Adipic acid from cyclohexane purified, cyclohexane oxidation route, with nitric acid ; production mix, at plant ; 1.36 g/cm3, 146 g/mol | CN | agg | Sphera |
Adiponitrile via direct hydrocyanation of Butadiene with hydrogen cyanide (prussic acid) ; single route, at plant ; 0.96 g/cm3, 108.14 g/mol | FR | agg | Sphera |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol ; single route, at plant ; estimation | DE | agg | Sphera |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol ; single route, at plant ; estimation | US | agg | Sphera |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol ; single route, at plant ; estimation | EU-28 | agg | Sphera |
Alfol Process (in Octanol production) hydrogenation, ethylation, chain growth, oxidation, hydrolysis ; single route, at plant ; 0.83 g/cm3, 130.23 g/mol | US | agg | Sphera |
Aliphatic polyisocyanate prepolymer (IPDI-based) polyaddition of isophorone diisocyanate and polyol ; production mix, at plant ; 80% isocyanates, 20% polyols | EU-28 | agg | Sphera |
Aliphatic polyisocyanate prepolymer (IPDI-based) polyaddition of isophorone diisocyanate and polyol ; production mix, at plant ; 80% isocyanates, 20% polyols | DE | agg | Sphera |
Alkali resistent (AR) glass fibres from mineral components ; single route, at plant ; SiO2 63%, ZrO2 16,5%, Na2O 15 %, CaO 5,5% | DE | agg | Sphera |
Alkali-Xanthate reaction of sodium hydroxide with alcohol and carbon disulphide ; production mix, at plant ; 144 g/mol in when ethanol and sodium hydroxide... | DE | agg | Sphera |
Alkyd resin (LM-system) condensation of polyols, polybasic acids or fatty acids ; single producer, at plant ; 27 MJ/ kg net calorific value | EU-28 | agg | Sphera |
Alkyd resin (LM-system) condensation of polyols, polybasic acids or fatty acids ; single route, at plant ; 27 MJ/kg net calorific value | DE | agg | Sphera |
Allyl alcohol from allyl chloride produced from nucleophilic substitution ; single route, at producer ; 58.08 g/mol | DE | agg | Sphera |
Allyl chloride (C3H5Cl), by-product hydrochloric acid (100%) chlorination of propene ; production mix, at plant ; 0.94 g/cm3, 76.53 g/mol | BE | agg | Sphera |
Allyl chloride (C3H5Cl), by-product hydrochloric acid (100%) chlorination of propene ; production mix, at plant ; 0.94 g/cm3, 76.53 g/mol | ES | agg | Sphera |
Allyl chloride (C3H5Cl), by-product hydrochloric acid (100%) chlorination of propene ; production mix, at plant ; 0.94 g/cm3, 76.53 g/mol | NL | agg | Sphera |
AlNiCo magnet (approximation) metals casting ; single route, at plant ; 55% ferrite, 10% aluminium, 15% nickel, 20% coba... | DE | agg | Sphera |
Alpaca fleece (washed) at harbour low intensity alpaca production system, farming, washing and transport from the farm to harbour ; production mix, at plant ; 50% carbon content | PE | agg | Sphera |
Alpha pinene (approximation) turpentine from kraft paper production, distillation of alpha-pinene ; single route, at producer ; 0.858 g/cm3, 136.24 g/mol | EU-28 | p-agg | Sphera |
Aluminium (AlMgSi10) powder ingot production, melting and atomizing with air jet ; single route, at plant ; AlMgSi10 | EU-28 | agg | Sphera |
Aluminium (paste; H2O content) Hydropor atomizing AL powder, ball milling ; single producer, at plant ; particle size around 5- 35 microns | DE | agg | Sphera |
Aluminium chloride (approximation) dissolving alumina in hydrochloric acid ; single route, at plant ; 2.44 g/cm3, 133.34 g/mol | DE | agg | Sphera |
Aluminium chloride (approximation) dissolving alumina in hydrochloric acid ; single route, at plant ; 2.44 g/cm3, 133.34 g/mol | EU-28 | agg | Sphera |
Aluminium chloride hexahydrate electrolytic reaction of aluminium and HCl ; single route, at plant ; 1.3 g/cm3, 241.43 g/mol | DE | agg | Sphera |
Aluminium diacetate (approximation) reaction of sodium aluminate and acetic acid ; production mix, at plant ; 162.1 g/mol | DE | agg | Sphera |
Aluminium extrusion profile (AlMg1SiCu) primary production ; production mix, at plant ; Alloy composition: 0.195%Cr, 0.275%Cu, 1%Mg, 0... | DE | agg | Sphera |
Aluminium flakes paste (chromated, 65% solids incl. solvents) wet milling process ; single route, at plant ; chromated, 65% solids | DE | agg | Sphera |
Aluminium flakes paste (chrome-free, 60% solids incl. solvents) wet milling process ; single route, at plant ; chrome-free, 60% solids | DE | agg | Sphera |
Aluminium fluoride reaction of bauxite, fluorspar and sulphuric acid ; production mix, at plant ; 2.88 g/cm3, 83.98 g/mol | EU-28 | agg | Sphera |
Aluminium Hydroxide from Bauxite Bayer process ; consumption mix, at plant ; 2.42 g/cm3, 78.00 g/mol | EU-28 | agg | Sphera |
Aluminium ingot (AlMgSc) - Sc2O3 approximation with Ru - best case 0,02% Sc (approximation) primary production ; production mix, at plant ; Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.1... | DE | agg | Sphera |
Aluminium ingot (AlMgSc) - Sc2O3 approximation with Ru - worst case 0,4% Sc (approximation) primary production ; production mix, at plant ; Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.1... | DE | agg | Sphera |
Aluminium ingot (AlMgSi10) primary production ; production mix, at plant ; AlMgSi10 | DE | agg | Sphera |
Aluminium ingot (AlTi5B1) primary production ; production mix, at plant ; Alloy composition: 0.1%Cu, 0.01%Mg, 0.2%Si, 5.... | DE | agg | Sphera |
Aluminium nitrate (approximation) reaction of aluminium hydroxide with nitric acid ; single route, at plant ; 1.72 g/cm3, 213 g/mol | EU-28 | agg | Sphera |
Aluminium particles/granules secondary production, remelting ; single route, at producer ; 2700 kg/m3 | EU-28 | agg | Sphera |
Aluminium Sandwich Foil processing of aluminium, polyethylene and glass fibres ; single route, at plant ; 69% aluminium, 8% polyethylene, 23% glass fibres | DE | agg | Sphera |
Aluminium sheet (AlMg4.5Mn0.4) primary production ; production mix, at plant ; Alloy composition: Cr 0,1%; Cu 0,15%; Mg 4,5 %... | DE | agg | Sphera |
Aluminium silicate (zeolite type A) from aluminum, silica, desired ions, and sodium hydroxide ; production mix, at plant ; 162.05 g/mol | DE | agg | Sphera |
Aluminium sulphate (approximation) from aluminium hydroxide and sulphuric acid ; single route, at plant ; 2.71 g/cm3, 342.15 g/mol | DE | agg | Sphera |
Aluminium sulphate (approximation) via aluminium hydroxide and sulphuric acid ; single route, at plant ; 2.71 g/cm3, 342.15 g/mol | EU-28 | agg | Sphera |
Aluminium sulphate (approximation) via aluminium hydroxide and sulphuric acid ; single route, at plant ; 2.71 g/cm3, 342.15 g/mol | US | agg | Sphera |
Aluminium sulphate from aluminium pig (approximation) via aluminium ingot and sulphuric acid ; single route, at plant ; 2.71 g/cm3, 342.15 g/mol | DE | agg | Sphera |
Aluminium Trilactate/Aluminium Lactate - open input corn seeds reaction of lactic acid with aluminium hydroxide ; production mix, at plant ; 294.19 g/mol | DE | p-agg | Sphera |
AlZn5Mg3Cu Sheet anodized aluminium profile production, anodizing ; single route, at plant ; 2.7 kg/m2 | DE | agg | Sphera |
Amine adduct emulsion on an aqueous base (approximation) polymerisation of a bisphenol A resin with a polyamine ; single route, at plant ; 55% polymer, 45% water | DE | agg | Sphera |
Amine adduct emulsion on an aqueous base (approximation) polymerisation of a bisphenol A resin with a polyamine ; single route, at plant ; 55% polymer, 45% water | EU-28 | agg | Sphera |
Amino trimethylene phosphonic acid (approximation) reaction of ammonium chloride, formaldehyde and phosphoric acid ; production mix, at plant ; 1.33 g/cm3, 299.05 g/mol | DE | agg | Sphera |
Amino trimethylene phosphonic acid, sodium salt (approximation) reaction of ammonium chloride, formaldehyde and phosphoric acid ; production mix, at plant ; 1.33 g/cm3, 299.05 g/mol | EU-28 | agg | Sphera |
Ammonia (high purity) purified with activated carbon ; single route, at plant ; 0.7714 kg/m3, 17.03 g/mol | DE | agg | Sphera |
Ammonia (NH3) synthesis with CO2 recovery, by-product carbon dioxide (without allocation) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | BE | p-agg | Sphera |
Ammonia (NH3) synthesis with CO2 recovery, by-product carbon dioxide (without allocation) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | JP | p-agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | JP | agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | BE | agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | CN | agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (economic allocation) Haber-Bosch process, from coal ; single route, at plant ; 0.7714 kg/m3, 17.03 g/mol | CN | agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (without allocation) Haber-Bosch process, from coal ; single route, at plant ; 0.7714 kg/m3, 17.03 g/mol | CN | p-agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | CN | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | AU | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | BE | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air) Haber-Bosch process, from natural gas ; production mix, at plant ; 0.7714 kg/m3, 17.03 g/mol | MY | agg | Sphera |
Ammonia liquid (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation) technology mix ; production mix, at plant ; liquid, agriculture | EU-28 | agg | Sphera |
Ammonia liquid (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation) technology mix ; production mix, at plant ; liquid, agriculture | CN | agg | Sphera |
Ammonia solution, NH3 (aq.) (approximation) Haber-Bosch process, from natural gas, diluted solution ; production mix, at plant ; 35% concentrated | EU-28 | agg | Sphera |
Ammonia water (weight share 25% NH3) ammonium mixed with water ; production mix, at plant ; weight share 25% NH3 | DE | agg | Sphera |
Ammonium bromide from bromine and ammonia ; single route, at plant ; 2.43 g/cm3, 97.94 g/mol | DE | agg | Sphera |
Ammonium chloride (salmiac, Solvay-process) Solvay process ; single route, at plant ; 1.53 g/cm3, 53.49 g/mol | EU-28 | agg | Sphera |
Ammonium hydrogen carbonate (Ammonium bicarbonate) reacting ammonia with CO2 ; single producer, at plant ; 1.59 g/cm3, 79.06 g/mol | EU-28 | agg | Sphera |
Ammonium hydrogen carbonate (Ammonium bicarbonate) reacting ammonia with CO2 ; single route, at plant ; 1.59 g/cm3, 79.06 g/mol | DE | agg | Sphera |
Ammonium nitrate (ON, BAT, 68% solution) from nitric acid ; production mix, at plant ; 1.73 g/cm3, 80.04 g/mol | AU | agg | Sphera |
Ammonium sulphate by-product acetone cyanhydrin (ACH) (approximation) with hydrogen cyanide from acrylonitrile by-product ; single route, at plant ; 1.77 g/cm3, 132.14 g/mol | EU-28 | agg | Sphera |
Ammonium sulphate by-product acrylonitrile (AN), hydrogen cyanide (mass allocated) propene ammoxidation, by- product acrylonitrile ; single route, at plant ; 1.77 g/cm3, 132.14 g/mol | DE | agg | Sphera |
Ammonium sulphate by-product Caprolactam from Cyclohexanone from Cyclohexane from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | BE | agg | Sphera |
Ammonium sulphate by-product Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; single route, at plant ; 1.77 g/cm3, 132.14 g/mol | NL | agg | Sphera |
Ammonium sulphate by-product Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; single route, at plant ; 1.77 g/cm3, 132.14 g/mol | EU-28 | agg | Sphera |
Ammonium sulphate mix (by-product), 50:50 technology mix ; production mix, at plant ; 1.77 g/cm3, 132.14 g/mol | EU-28 | agg | Sphera |
Ammonium sulphate, by product acrylonitrile, hydrocyanic acid propene ammoxidation, by- product acrylonitrile ; single route, at plant ; 1.77 g/cm3, 132.14 g/mol | DE | agg | Sphera |
Ammoniumpolyphosphate from urea and phoshoric acid ; production mix, at plant ; 1,9 g/cm3, 97.01 g/mol | DE | agg | Sphera |
Anhydrite (CaSO4) (natural) technology mix (mining and open pit mining) ; production mix, at producer ; 2.96 g/cm3 | DE | agg | Sphera |
Anhydrite (CaSO4) (natural) (EN15804 A1-A3) technology mix (mining and open pit mining) ; production mix, at producer ; 2.96 g/cm3 | EU-28 | agg | Sphera |
Anhydrite (CaSO4) (thermal) (EN15804 A1-A3) thermal produced anhydrite ; production mix, at plant ; grinded and purified product | EU-28 | agg | Sphera |
Aniline (phenyl amine, amino benzene) catalytic hydrogenation of nitrobenzene ; single route, at plant ; 1.022 g/cm3, 93.13 g/mol | BR | agg | Sphera |
Aniline (phenyl amine, amino benzene) catalytic hydrogenation of nitrobenzene ; single route, at plant ; 1.02 g/cm3, 93 g/mol | CN | agg | Sphera |
Anthraquinone via naphthalene via naphthalene ; single route, at plant ; 1.31 g/cm3, 208.22 g/mol | DE | agg | Sphera |
Anthraquinone via reformate via reformate from pyrolysis gas ; single route, at plant ; 1.31 g/cm3, 208.22 g/mol | DE | agg | Sphera |
Antimony (Blast furnace route) primary production, open pit mining, blast furnace processing ; single route, at plant ; 90% Antimony | CN | agg | Sphera |
Antimony (Hydrometallurgy route) primary production, open pit mining, hydrometallurgical processing ; single route, at plant ; 98.5% Antimony, cathode metal | CN | agg | Sphera |
Antimony trioxide primary production, antimony ore mining, roasting ; single route, at plant ; 5.2 g/cm3, 291.5 g/mol | EU-28 | agg | Sphera |
Apple plantation (85% H2O content) Apple cultivation ; production mix, at field border ; Apples at field, 85% H20 | CN | agg | Sphera |
Application primer (waterproof) water proof application ; single route, at plant ; application per m2 | US | agg | Sphera |
Application primer (waterproof) water proof application ; single route, at plant ; application per m2 | EU-28 | agg | Sphera |
Aramide fiber (para aramid) condensation of para- phenylene diamine and terephthaloyl dichloride ; single route, at plant ; para aramid | DE | agg | Sphera |
Argon (gaseous) cryogenic air fractionation ; production mix, at plant ; 40 g/mol | CN | agg | Sphera |
Argon (highly pure) Linde process, cryogenic air fractionation ; production mix, at plant ; 40 g/mol | US | agg | Sphera |
Aromatics (BTX) at refinery from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | MY | agg | Sphera |
Aromatics (BTX) at refinery from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | RU | agg | Sphera |
Aromatics (BTX) at refinery from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | NL | agg | Sphera |
Ascorbic acid Reichstein Synthesis, from glucose ; single route, at plant ; 1.65 g/cm3, 176.12 g/mol | DE | agg | Sphera |
Asphalt binder (rolling asphalt) combination of aggregates and bitumen ; production mix, at plant ; 170 - 250 kg/m2 | DE | agg | Sphera |
Average load of laundry (load 1 lb/ 0.4536 kg) - open input textiles average washing machine, for domestic textile cleaning ; production mix, at plant ; energy consumption 2.25 kWh/ load, water consu... | US | p-agg | Sphera |
Average load of laundry (load 10 lb/4.536 kg) - open input textiles average washing machine, for domestic textile cleaning ; production mix, at plant ; energy consumption 2.25 kWh/ load, water consu... | US | p-agg | Sphera |
Average load of laundry (load 20 lb/9.072 kg) - open input textiles average washing machine, for domestic textile cleaning ; production mix, at plant ; energy consumption 2.25 kWh/ load, water consu... | US | p-agg | Sphera |
Average Printed Wiring Board with Power Electronics (DfX-compatible) production of power electronics on base of FR4 substrate ; single route, at producer ; 0,01 sqm | GLO | agg | Sphera |
Average Printed Wiring Board with Signal Electronics (DfX-compatible) Production of signal electronics on base of FR4 substrate ; single route, at producer ; 0,01 sqm | GLO | agg | Sphera |
Average Printed Wiring Board with Signal-Power Electronics (DfX-Compatible) Production of signal-power electronics on base of FR4 substrate ; single route, at producer ; 0,01 sqm | GLO | agg | Sphera |
Azodicarbonamide (propellant) from hydrazine and urea ; single route, at plant ; 1.65 g/cm3, 116.08 g/mol | DE | agg | Sphera |
Bamboo cultivation (80% H2O content) technology mix ; production mix, at producer ; 80% H2O | CN | agg | Sphera |
Barge, 1,500t payload capacity / canal technology mix, diesel driven, cargo ; consumption mix, to consumer ; 1,500t payload capacity/ canal | GLO | u-so | Sphera |
Barium carbonate via barium sulfide and CO2 reaction of barium sulfide solution with CO2, precipitation of barium carbonate ; single route, at plant ; 4.43 g/cm3 at 20°C, 197.34 g/mol | DE | agg | Sphera |
Barium chloride (approximation) reaction of barium sulphide and hydrochloric acid ; production mix, at plant ; 3.86 g/cm3, 208.23 g/mol | DE | agg | Sphera |
Barium hydroxide (approximation) reaction of barium sulphide and sodium hydroxide ; single route, at plant ; 3.74 g/cm3, 171.34 g/mol | EU-28 | agg | Sphera |
Barium magnesium aluminate (BAM), europium doped from Al2O3, BaCO3, MgCO3, and Eu2O3 ; single route, at plant ; 1202 g/mol | GLO | agg | Sphera |
Barium sulphate (BaSO4) carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate ; production mix, at plant ; 4.5 g/cm3, 233.43 g/mol | DE | agg | Sphera |
Barium sulphate (BaSO4) carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate ; production mix, at plant ; 4.5 g/cm3, 233.43 g/mol | US | agg | Sphera |
Barium sulphate (BaSO4) carbothermal reduction of barium sulphate to barium sulphide, reaction with sodium sulphate ; production mix, at plant ; 4.5 g/cm3, 233.43 g/mol | EU-28 | agg | Sphera |
Barium sulphide (100%) carbothermal reduction of barium sulphate ; production mix, at plant ; 4.25 g/cm3, 169.39 g/mol | DE | agg | Sphera |
Barium zinc stearate (stabiliser, approximation) production of barium stearate and zinc stearate, mixing ; production mix, at plant ; 60% barium stearate, 40% zinc stearate, 63.1% ... | EU-28 | agg | Sphera |
Basalt production (washed) basalt mining and crushing ; single producer, at plant ; <52% SiO2 | EU-28 | agg | Sphera |
Basalt production (washed) basalt mining and crushing ; single producer, at plant ; <52% SiO2 | DE | agg | Sphera |
Base oil (group I) (solvent refined) from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | EU-28 | agg | Sphera |
Base oil (group II) (hydrotreated) from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | EU-28 | agg | Sphera |
Base oil (group III) (hydrocracked) from crude oil ; production mix, at refinery ; 40 MJ/kg net calorific value | EU-28 | agg | Sphera |
Beech industrial wood (25 % moisture content, 20 % H2O content) Forest cultivation, plantation maintanance ; production mix, at producer ; 25% moisture, 20% H2O content included in w... | EU-28 | agg | Sphera |
Beech log free forest track (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 660 kg/m3, 0 % moisture content / 0 % H2O cont... | DE | agg | Sphera |
Beech log free forest track (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 0 % moisture content, 0 % H2O content | CN | agg | Sphera |
Beech log free forest track (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 0 % moisture content, 0 % H2O content | US | agg | Sphera |
Beech log free forest track (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 660 kg/m3, 0 % moisture content, 0 % H2O conte... | EU-28 | agg | Sphera |
Beech log free forest track (25 % moisture content, 20 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 25% moisture, 20% H2O content included in wood | EU-28 | agg | Sphera |
Beef filet (cattle slaughterhouse) (economic allocation) slaughterhouse ; single producer, at plant ; boneless beef filet, 13.5% carbon content | DE | agg | Sphera |
Bentonite, natural mining and beneficiation ; production mix, at plant ; composed primarily of smectite minerals | DE | agg | Sphera |
Bentonite, natural mining and beneficiation ; production mix, at plant ; composed primarily of smectite minerals | EU-28 | agg | Sphera |
Bentonite, natural mining and beneficiation ; production mix, at plant ; composed primarily of smectite minerals | IN | agg | Sphera |
Bentonite, natural mining and beneficiation ; production mix, at plant ; composed primarily of smectite minerals | CN | agg | Sphera |
Bentonite, natural mining and beneficiation ; production mix, at plant ; composed primarily of smectite minerals | RU | agg | Sphera |
Benzaldehyde via benzal chloride ; single route, at producer ; 1.04 g/cm3, 106.12 g/mol | EU-28 | agg | Sphera |
Benzanthrone from sulphuric acid and anthrone ; single route, at plant ; 230.27 g/mol | US | agg | Sphera |
Benzene (from pyrolysis gasoline) from pyrolysis fuel ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | ES | agg | Sphera |
Benzene by-product BTX (from reformate) from reformate ; single route, at plant ; 0.88 g/cm3, 78.1 g/mol | BR | agg | Sphera |
Benzene by-product BTX (from reformate) (approximation) from reformate ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | CN | agg | Sphera |
Benzene by-product BTX (from reformate) (approximation) from reformate ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | TH | agg | Sphera |
Benzene by-product ethyne (acetylene) Sachsse Bartholome Process ; single route, at plant ; 0.88 g/cm3, 78 g/mol | DE | agg | Sphera |
Benzene from hard coal from hard coal ; single route, at plant ; 0.88 g/cm3, 78 g/mol | EU-28 | agg | Sphera |
Benzene from hard coal from hard coal ; single route, at plant ; 0.88 g/cm3, 78 g/mol | NL | agg | Sphera |
Benzene from hard coal from hard coal ; single route, at plant ; 0.88 g/cm3, 78 g/mol | DE | agg | Sphera |
Benzene from hard coal (from DE Coke mix) from hard coal ; single route, at plant ; 0.88 g/cm3, 78 g/mol | US | agg | Sphera |
Benzene mix technology mix ; production mix, at plant ; 0.88 g/cm3, 78.1 g/mol, 40.57 MJ/kg | CN | agg | Sphera |
Benzene sulfonic acid sulfonation of benzene ; single route, at plant ; 1.32 g/cm3 (47 °C), 158.18 g/mol | DE | agg | Sphera |
Benzene sulfonic acid (approximation) sulfonation of benzene ; single producer, at plant ; 1.32 g/cm3 (47 °C), 158.18 g/mol | EU-28 | agg | Sphera |
Benzene sulfonic acid (approximation) sulfonation of benzene ; single producer, at plant ; 1.32 g/cm3 (47 °C), 158.18 g/mol | US | agg | Sphera |
Benzenesulfonyl chloride (approximation) Chlorination of Benzence Sulfonic Acid with Phosphorous Oxychloride Method, liquid phase reaction, distillation ; Single route, at producer ; liquid, 176.62 g/mol; 1.384 g/mL at 25°C | DE | agg | Sphera |
Benzoic acid ester esterification of hydroxybenzoic acid with ethanol ; production mix, at plant ; 166 g/mol | DE | agg | Sphera |
Benzoic acid ester esterification of hydroxybenzoic acid with ethanol ; production mix, at plant ; 166 g/mol | EU-28 | agg | Sphera |
Benzotrichloride (approximation) chlorination of toluene ; production mix, at plant ; 1.38 g/cm3, 195.48 g/mol | US | agg | Sphera |
Benzoyl Chloride (approximation) reaction of benzoyl trichloride with water ; single route, at plant ; 1.21 g/cm3, 140.57 g/mol | US | agg | Sphera |
Benzoyl Peroxide production from benzoyl chloride and hydrogen peroxide ; production mix, at plant ; 1.33 g/cm3, 242.23 g/mol | US | agg | Sphera |
Benzyl alcohol hydrolysis of benzyl chloride ; single route, at plant ; 1.04 g/cm3, 108.14 g/mol | EU-28 | agg | Sphera |
Benzyl alcohol in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 34.6 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Benzyl chloride (α-Chlorotoluene) chlorination of toluene ; single route, at plant ; 1.21 g/cm3, 140.57 g/mol | EU-28 | agg | Sphera |
Beta pinene (approximation) turpentine from kraft paper production, distillation of beta-pinene ; single route, at producer ; 0.872 g/cm3, 136.24 g·mol−1 | EU-28 | p-agg | Sphera |
BF Cold rolled coil blast furnace route ; single route, at plant ; carbon steel, 1.02 mm thickness | EU-28 | p-agg | Sphera |
BF slag incl. grinding BF route ; production mix and grinding, at plant ; assemblage of Ca-Al-Mg silicates | AE | agg | Sphera |
BF Steel billet (14 CrMoV6 9) BF route ; production mix, at plant ; Crude steel, 14 CrMoV6 9 | DE | agg | Sphera |
BF Steel billet / slab / bloom blast furnace route ; single route, at plant ; carbon steel | EU-28 | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR1 (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR160IF (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR180BH (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR180IF (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR2 (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210BH (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210IF (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR210LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240BH (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240IF (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR240LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,02... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR270LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR290Y490T-DP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR3 (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR300LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR330Y590T-DP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR340LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR380LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR4 (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR400Y690T-TR (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR420LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR440Y780T-DP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR450Y780T-TR (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR460LA (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR5 (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR570Y780T-CP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR590Y980T-DP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,01... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR700Y980T-DP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR780Y980T-CP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; CR900Y1180T-CP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; EG 2-sides; 1 mm; HR660Y760T-CP (VDA) BF Steel sheet; cold rolled; EG ; production mix, at producer ; C 0,18 %; Si 1 %; Mn 2,52%; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR1 (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR160IF (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR180BH (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR180IF (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR2 (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210BH (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210IF (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR210LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240BH (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240IF (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR240LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,02... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR270LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR290Y490T-DP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR3 (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR300LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR330Y590T-DP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR340LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR380LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR4 (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR400Y690T-TR (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR420LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR440Y780T-DP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR450Y780T-TR (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR460LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR5 (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR500LA (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,12 %; Si 0,6 %; Mn 1,7 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR570Y780T-CP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR590Y980T-DP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,01... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR700Y980T-DP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR780Y980T-CP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; HDG 2-sides; 1 mm; CR900Y1180T-CP (VDA) BF Steel sheet; cold rolled; HDG ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; 14 CrMoV6 9 BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; 14 CrMoV6 9 | DE | agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR1 (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 0,6 %; P 0,065 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR160IF (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,6 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR180BH (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR180IF (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,7 %; P 0,06 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR2 (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 0,5 %; P 0,065 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR210BH (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,7 %; P 0,85 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR210IF (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 0,9 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR210LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,08 %; S 0,03... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR240BH (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,1 %; S 0,03 ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR240IF (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,01 %; Si 0,3 %; Mn 1,6 %; P 0,1 %; S 0,... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR240LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,1 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,02... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR270LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1 %; P 0,03 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR290Y490T-DP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,14 %; Si 0,5 %; Mn 1,8 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR3 (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,08 %; Si 0,5 %; Mn 0,5 %; P 0,003 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR300LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,4 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR330Y590T-DP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,15 %; Si 0,75 %; Mn 2,5 %; P 0,04 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR340LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,5 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR380LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,6 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR4 (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,06 %; Si 0,5 %; Mn 0,4 %; P 0,025 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR400Y690T-TR (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,24 %; Si 2 %; Mn 2,2 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR420LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,65 %; P 0,03 %; S ... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR440Y780T-DP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,18 %; Si 0,8 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR450Y780T-TR (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,25 %; Si 2,2 %; Mn 2,5 %; P 0,08 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR460LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,5 %; Mn 1,7 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR5 (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,02 %; Si 0,5 %; Mn 0,3 %; P 0,02 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR500LA (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,12 %; Si 0,6 %; Mn 1,7 %; P 0,03 %; S 0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR570Y780T-CP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,18 %; Si 1 %; Mn 2,5 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR590Y980T-DP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,2 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,01... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR700Y980T-DP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR780Y980T-CP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,7 %; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; CR900Y1180T-CP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,23 %; Si 1 %; Mn 2,9 %; P 0,04 %; S 0,0... | DE | p-agg | Sphera |
BF Steel sheet; cold rolled; uncoated; 1 mm; HR660Y760T-CP (VDA) BF Steel sheet; cold rolled; uncoated ; production mix, at producer ; C 0,18 %; Si 1 %; Mn 2,52%; P 0,08 %; S 0,0... | DE | p-agg | Sphera |
BF Tin-free Steel coil blast furnace route ; single route, at plant ; carbon steel, 1.02 mm thickness | EU-28 | p-agg | Sphera |
BF Tinplate coil blast furnace route ; single route, at plant ; carbon steel, 1.02 mm thickness | DE | p-agg | Sphera |
BF Tinplate coil blast furnace route ; single route, at plant ; carbon steel, 1.02 mm thickness | EU-28 | p-agg | Sphera |
Biaxial oriented PA film (BOPA PA6) polyamide 6 extrusion and stretching ; single route, at plant ; 32 MJ/kg net calorific value | DE | agg | Sphera |
Biaxial oriented PET film (BOPET) PET extrusion and stretching ; single route, at plant ; 1.38 g/cm3, 192.17 g/mol per repeating unit, 32 ... | DE | agg | Sphera |
Biaxial oriented polypropylene film (BOPP) polypropylene extrusion and stretching ; single producer, at plant ; 44 MJ/kg net calorific value | DE | agg | Sphera |
Biaxial oriented polypropylene film (BOPP) polypropylene extrusion and stretching ; single producer, at plant ; 44 MJ/kg net calorific value | US | agg | Sphera |
Biaxial oriented Polystyrene film (BOPS) polystyrene extrusion and stretching ; single route, at plant ; 40 MJ/kg net calorific value | DE | agg | Sphera |
Bicomponent fiber (PET/PA) spinning of polyethylene terephthalate, polyamide and epoxy resin ; production mix, at plant ; 85% PET, 15% PA | DE | agg | Sphera |
Biobased Polyol from canola oil technology mix, transesterification, epoxidation, ring opening ; production mix, at producer ; from rapeseed | EU-28 | agg | Sphera |
Biobased Polyol from corn oil technology mix, transesterification, epoxidation, ring opening ; production mix, at producer ; from corn | US | agg | Sphera |
Biodiesel based on rape seed methyl ester (RME) from rape seeds ; production mix, at plant ; 78% total carbon content, 74% biogenic carbon ... | EU-28 | agg | Sphera |
Bioethanol (from corn) from corn ; production mix, at plant ; 55% carbon content, 26.8 MJ net calorific value | EU-28 | agg | Sphera |
Bioethanol from sugar beet, at plant from sugar beet ; production mix, at plant ; 52% carbon content, 26.8 MJ net calorific value | EU-28 | agg | Sphera |
Bioethanol from sugar beet, at plant from sugar beet ; single route, at plant ; 0.79 g/cm3, 46.07 g/mol | DE | agg | Sphera |
Bioethanol from sugar cane (no slash and burn) (approx. energy credits) from sugar cane ; single route, at plant ; 0.79 g/cm3, 46.07 g/mol | BR | agg | Sphera |
Bioethanol from sugar cane, at plant from sugar cane ; production mix, at plant ; 52% carbon content, 26.8 MJ net calorific value | BR | agg | Sphera |
Bioethanol from wheat (DDGS internal energy) from wheat ; single route, at plant ; 0.79 g/cm3, 46.07 g/mol | EU-28 | agg | Sphera |
Bioethanol from wheat, at plant transport, conditioning and fermentation of wheat ; single route, at plant ; 55% carbon content, 26.8 MJ net calorific value | EU-28 | agg | Sphera |
Biogas for bioenergy technology mix ; consumption mix, to consumer ; 15.1 MJ/kg net calorific value | NL | agg | Sphera |
Biogas for bioenergy technology mix ; consumption mix, to consumer ; 15.1 MJ/kg net calorifiv value | GB | agg | Sphera |
Biogas for bioenergy technology mix ; consumption mix, to consumer ; 15.1 MJ/kg net calorific value | DE | agg | Sphera |
Biogas from cattle liquid manure Anaerobic wet fermentation ; production mix, at plant ; 15,37 MJ/kg; 1,28 kg/m3; CH4 content: 55 % vol... | DE | p-agg | Sphera |
Biogas from cattle paunch contents technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 59% methane content, 36 Mj/m3 net calorific va... | DE | p-agg | Sphera |
Biogas from cattle solid manure Anaerobic wet fermentation ; production mix, at plant ; 17,63 MJ/kg; 1,22 kg/m3; CH4 content: 60 % vol... | DE | p-agg | Sphera |
Biogas from flotate sludge technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 59% methane content, 36 Mj/m3 net calorific va... | DE | p-agg | Sphera |
Biogas from kitchen residues Anaerobic wet fermentation ; production mix, at plant ; 17,73 MJ/kg; 1,22 kg/m3; CH4 content: 60 % vol... | DE | p-agg | Sphera |
Biogas from maize silage - open input biomass (corn grains) - 1MJ Anaerobic wet fermentation ; production mix, at plant ; 14,16 MJ/kg; 1,32 kg/m3; CH4 content: 52 % vol... | DE | p-agg | Sphera |
Biogas from maize silage - open input biomass (corn grains) - 1kg Anaerobic wet fermentation ; production mix, at plant ; 14,16 MJ/kg; 1,32 kg/m3; CH4 content: 52 % vol... | DE | p-agg | Sphera |
Biogas from municipal organic waste Anaerobic wet fermentation ; production mix, at plant ; 17,63 MJ/kg; 1,22 kg/m3; CH4 content: 60 % vol... | DE | p-agg | Sphera |
Biogas from organic waste mix technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 59% methane content, 36 Mj/m3 net calorific va... | DE | p-agg | Sphera |
Biogas from pig liquid manure Anaerobic wet fermentation ; production mix, at plant ; 17,63 MJ/kg; 1,22 kg/m3; CH4 content: 60 % vol... | DE | p-agg | Sphera |
Biogas from poultry solid manure Anaerobic wet fermentation ; production mix, at plant ; 20,14 MJ/kg; 1,16 kg/m3; CH4 content: 65 % vol... | DE | p-agg | Sphera |
Biogas from sewage sludge - 1MJ Anaerobic wet fermentation ; production mix, at plant ; 17,18 MJ/kg; 1,22 kg/m3; CH4 content: 60 % vol... | DE | p-agg | Sphera |
Biogas from sugar beet leaves Anaerobic wet fermentation ; production mix, at plant ; 15,07 MJ/kg; 1,29 kg/m3; CH4 content: 54 % vol... | DE | p-agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.46 MJ/kg net calorific value | PT | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.46 MJ/kg net calorific value | FI | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 11.46 MJ/kg net calorific value | TH | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.51 MJ/kg net calorific value | DK | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.07 MJ/kg net calorific value | HU | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.7 MJ/kg net calorific value | CA | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.71 MJ/kg net calorific value | NL | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.55 MJ/kg net calorific value | GB | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.52 MJ/kg net calorific value | NZ | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.43 MJ/kg net calorific value | DE | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 9.81 MJ/kg net calorific value | BR | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.84 MJ/kg net calorific value | SE | agg | Sphera |
Biomass (solid) for bioenergy technology mix ; consumption mix, to consumer ; 14.56 MJ/kg net calorific value | US | agg | Sphera |
Biomass Power Plant - CHP (lumber, 12% moisture) cogeneration electricity and heat, technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 15.84 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Biomethane from cattle liquid manure technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from cattle liquid manure -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from cattle liquid manure, 56% from external and 44% self-supply electricity technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from cattle paunch contents technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from cattle solid manure technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from distiller's wash, 56% from external and 44% self-supply electricity technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from flotate sludge technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from flotate sludge -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from flotate sludge, 56% from external and 44% self-supply electricity technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from glycerine -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from hop vine chips -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of hop vine to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from kitchen residues technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from kitchen residues -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from municipal organic waste technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from organic waste mix technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from pig liquid manure technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from pig liquid manure -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from pig liquid manure, 56% from external and 44% self-supply electricity technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from pig solid manure technology mix / anaerobic fermentation of organic wastes to biomethane via wet fermentation prosess ; production mix, at plant ; 1MJ of biomethane | DE | p-agg | Sphera |
Biomethane from pig solid manure -80% RED value (16,76 GHG/MJ) technology mix / anaerobic fermentation of organic wastes to biomethane via wet fermentation prosess ; production mix, at plant ; 1MJ of biomethane | DE | p-agg | Sphera |
Biomethane from poultry solid manure technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from poultry solid manure -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of poultry organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from residues of protein feed production -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from sugar beet leaves technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from sugar beet leaves -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane from sugar beet pellets -80% RED value (16,76 g GHG/MJ) technology mix/ anaerobic fermentation of different organic matter to biogas via wet fermentation ; production mix, at plant ; 97,8% methane | DE | p-agg | Sphera |
Biomethane mix technology mix, different substrates ; production mix, at producer ; 74.9% carbon content, 48.9 MJ/kg net calori... | FR | p-agg | Sphera |
Bionaphtha from Palm Oil Mill Effluent (POME) recovery, transport, pretreatment and hydrotreatment (HVO process) of palm oil mill effluent (POME) oil ; single route, at producer ; 44 MJ/kg, 0.825 kg C/kg | EU-28 | agg | Sphera |
Bitumen at refinery from crude oil ; production mix, at refinery ; 38.71 MJ/kg net calorific value | NL | agg | Sphera |
Bitumen at refinery from crude oil ; production mix, at refinery ; 38.71 MJ/kg net calorific value | RU | agg | Sphera |
Bitumen at refinery from crude oil ; production mix, at refinery ; 38.71 MJ/kg net calorific value | MY | agg | Sphera |
Blood from pig, unprocessed, from slaughterhouse (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | EU-28 | agg | Sphera |
Blood meal from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Blood meal from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Blood meal from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Blood meal from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Blood meal from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Blood meal from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Blood meal from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | EU-28 | agg | Sphera |
Blood meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Blood meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Blood meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | ZA | agg | Sphera |
Blood meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Boiler ash from hard coal power plant from hard coal power plant ; production mix, at power plant ; grain size ca. 13 mm | EU-28 | agg | Sphera |
Boiler ash from hard coal power plant from hard coal power plant ; production mix, at power plant ; grain size ca. 13 mm | DE | agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | p-agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | p-agg | Sphera |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | p-agg | Sphera |
Boneless pork, from slaughterhouse (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | EU-28 | agg | Sphera |
Borax (dehydrated) via dehydration ; production mix, at plant ; 201.37 g/mol | EU-28 | agg | Sphera |
Borax (dehydrated) via dehydration ; production mix, at plant ; 201.37 g/mol | DE | agg | Sphera |
Borax pentahydrate via colemanite ; production mix, at plant ; 291 g/mol | EU-28 | agg | Sphera |
Borax pentahydrate via colemanite ; production mix, at plant ; 291 g/mol | DE | agg | Sphera |
Boric acid by-product sodium sulfate (approximation) reaction of borax pentahydrate and sulfuric acid ; single route, at plant ; 1.44 g/cm3, 61.83 g/mol | US | agg | Sphera |
Boric acid by-product sodium sulfate (approximation) reaction of borax pentahydrate and sulfuric acid ; single route, at plant ; 1.44 g/cm3, 61.83 g/mol | EU-28 | agg | Sphera |
Boric acid by-product sodium sulfate (approximation) reaction of borax pentahydrate and sulfuric acid ; single route, at plant ; 1.44 g/cm3, 61.83 g/mol | DE | agg | Sphera |
Brass (CuZn30) anode furnace and casting, mainly from brass scrap, secondary production ; single route, at plant ; 70% copper, 30% zinc | EU-28 | p-agg | Sphera |
Brass die-casting (CuZn20) die casting, mainly from brass scrap, secondary production ; single route, at plant ; 80% copper, 20% zinc | DE | p-agg | Sphera |
Bromine (from sea water) from sea water ; single route, at plant ; 3.10 g/cm3, 79.90 g/cm3 | EU-28 | agg | Sphera |
Bromine (from sea water) approximation from sea water ; single route, at plant ; 3.10 g/cm3, 79.90 g/cm3 | GB | agg | Sphera |
Bulk Moulding Compound Resin Mat (BMC) bulk moulding ; single route, at plant ; 18% polyester resin, 68% limestone, 12% glass fi... | DE | agg | Sphera |
Bunker oil at refinery from crude oil ; production mix, at refinery ; 3.5 wt.% sulphur | NL | agg | Sphera |
Bunker oil at refinery from crude oil ; production mix, at refinery ; 3.5 wt.% sulphur | MY | agg | Sphera |
Bunker oil at refinery from crude oil ; production mix, at refinery ; 3.5 wt.% sulphur | RU | agg | Sphera |
Butane at refinery from crude oil ; production mix, at refinery ; 45.76 MJ/kg net calorific value | RU | agg | Sphera |
Butane at refinery from crude oil ; production mix, at refinery ; 45.76 MJ/kg net calorific value | MY | agg | Sphera |
Butane at refinery from crude oil ; production mix, at refinery ; 45.76 MJ/kg net calorific value | NL | agg | Sphera |
Butane diamine ( Tetramethylenediamine TMDA) (approximation) reaction of acrylonitrile, hydrogen cyanide and hydrogen ; single route, at plant ; 0.88 g/cm3, 88.15 g/mol | CN | agg | Sphera |
Butane diamine (Tetramethylenediamine TMDA) reaction of acrylonitrile, hydrogen cyanide and hydrogen ; single route, at plant ; 0.88 g/cm3, 88.15 g/mol | DE | agg | Sphera |
Butane mix technology mix ; production mix, at plant ; 2.48 kg/m3, 58.12 g/mol | JP | agg | Sphera |
Butane mix technology mix ; production mix, at plant ; 2.48 kg/m3, 58.12 g/mol | DE | agg | Sphera |
Butanediol from acetylene (H2 via steam reforming of hard coal) Reppe chemistry process, from acetylene and formaldehyde ; production mix, at plant ; 1.02 g/cm3, 90 g/mol | CN | agg | Sphera |
Butanediol from acetylene (H2 via steam reforming of natural gas) Reppe chemistry process, from acetylene and formaldehyde ; single route, at plant ; 1.02 g/cm3, 90.12 g/mol | US | agg | Sphera |
Butanediol from acetylene (H2 via steam reforming of natural gas) Reppe chemistry process, from acetylene and formaldehyde ; production mix, at plant ; 1.02 g/cm3, 90 g/mol | CN | agg | Sphera |
Butanediol from maleic anhydride from maleic anhydride ; single route, at plant ; 1.02 g/cm3, 90.12 g/mol | US | agg | Sphera |
Butanediol from n-butane via maleic acid hydrogeneration via maleic acid hydrogeneration ; single route, at plant ; 1.02 g/cm3, 90.12 g/mol | US | agg | Sphera |
Butanol (n-butanol) from propylene with rhodium catalyst Oxo synthesis, from propylene with rhodium catalyst ; production mix, at producer ; 0.81 g/cm3, 74.12 g/mol | CN | agg | Sphera |
Butanol (n-butanol) from propylene with rhodium catalyst Oxo synthesis, from propylene with rhodium catalyst ; production mix, at producer ; 0.81 g/cm3, 74.12 g/mol | BR | agg | Sphera |
Butanol (n-butanol) from propylene with rhodium catalyst Oxo synthesis, from propylene with rhodium catalyst ; production mix, at producer ; 0.81 g/cm3, 74.12 g/mol | EU-28 | agg | Sphera |
Butanol (n-butanol) from propylene with rhodium catalyst Oxo synthesis, from propylene with rhodium catalyst ; production mix, at producer ; 0.81 g/cm3, 74.12 g/mol | DE | agg | Sphera |
Butene mix technology mix ; production mix, at plant ; 40 g/mol | EU-28 | agg | Sphera |
Butene mix technology mix ; production mix, at plant ; 40 g/mol | DE | agg | Sphera |
Butene-1 from C4 raffinate ; production mix, at plant ; 40 g/mol | DE | agg | Sphera |
Butyl acetate Fischer esterification ; production mix, at plant ; 0.88 g/cm3, 116.16 g/mol | CN | agg | Sphera |
Butyl acetate Fischer esterification ; production mix, at plant ; 0.88 g/cm3, 116.16 g/mol | US | agg | Sphera |
Butyl acetate Fischer esterification ; production mix, at plant ; 0.88 g/cm3, 116.16 g/mol | EU-28 | agg | Sphera |
Butyl acetate Fischer esterification ; production mix, at plant ; 0.88 g/cm3, 116.16 g/mol | DE | agg | Sphera |
Butyl acrylate esterification of acrylic acid and butanol ; single route, at plant ; density 0,90 g·cm−3, molar mass 128,17 g·mol−1 | CN | agg | Sphera |
Butyl acrylate esterification of acrylic acid and butanol ; single route, at plant ; density 0,90 g·cm−3, molar mass 128,17 g·mol−1 | DE | agg | Sphera |
Butyl acrylate esterification of acrylic acid and butanol ; single route, at plant ; density 0,90 g·cm−3, molar mass 128,17 g·mol−1 | EU-28 | agg | Sphera |
Butyl hydroxytoluene (BHT) via isobutene and cresol ; production mix, at plant ; 1.05 g/cm³, 220.35 g/mol | US | agg | Sphera |
Butyl hydroxytoluene (BHT) via isobutene and cresol ; production mix, at plant ; 1.05 g/cm³, 220.35 g/mol | DE | agg | Sphera |
Butyl peroxide oxidation of isobutane with oxygen ; single route, at plant ; 0.79 g/cm3, 146.23 g/mol | DE | agg | Sphera |
Butyl peroxide oxidation of isobutane with oxygen ; single route, at plant ; 0.79 g/cm3, 146.23 g/mol | JP | agg | Sphera |
Butylamine (n-butylamine from butanol) from butanol ; production mix, at plant ; 0.74 g/cm3, 73.14 g/mol | DE | agg | Sphera |
Butyldiglycol ethoxylation of butanol ; production mix, at plant ; liquid, density: 0,95 g·cm−3, molar mass: 162,... | DE | agg | Sphera |
Butyldiglycol acetate (approximation) from butyldiglycol and butyl acetate ; single route, at plant ; 0.98 gcm-3 at 20°C, 104.27 g/mol | DE | agg | Sphera |
Butylene at refinery from crude oil ; production mix, at refinery ; 45.51 MJ/kg net calorific value | MY | agg | Sphera |
Butylene at refinery from crude oil ; production mix, at refinery ; 45.51 MJ/kg net calorific value | RU | agg | Sphera |
Butylene at refinery from crude oil ; production mix, at refinery ; 45.51 MJ/kg net calorific value | NL | agg | Sphera |
Butylglycol reaction of ethylene oxide and butanol ; production mix, at plant ; 0.90 g/cm3, 118.18 g/mol | DE | agg | Sphera |
Butylglycol reaction of ethylene oxide and butanol ; production mix, at plant ; 0.90 g/cm3, 118.18 g/mol | EU-28 | agg | Sphera |
Butylisocyanat (N-Butyl isocyanat) reaction of phosgene with n-butylamine ; production mix, at plant ; 0,89 g/cm3, 99.13 g/mol | DE | agg | Sphera |
Butyric acid (Butanoic acid) by aldehyde oxidation oxidation of butyraldehyde ; single route, at plant ; 0.95 g/cm3, 88.11 g/mol | DE | agg | Sphera |
Butyric acid anhydride liquid- phase oxidation of butyraldehyde ; single route, at plant ; 0.967 g/cm3, molar mass 158.19 g/mol | DE | agg | Sphera |
Butyrolactone (from Butanediol) Reppe process, dehydrogenation of butanediol ; single route, at plant ; 1.13 g/cm3, 86.09 g/mol | DE | agg | Sphera |
Butyrolactone (from maleic anhydride) from maleic anhydride ; single route, at plant ; 1.13 g/cm3, 86.09 g/mol | DE | agg | Sphera |
C10-Methylester including transesterification and fractionation Crude coconut oil processing, transesterification and fractionation ; single producer, at plant ; C10 methyl ester fraction, 71% carbon content | MY | agg | Sphera |
C12-Methylester including transesterification and fractionation Palm kernel oil processing, transesterification and fractionation ; single producer, at plant ; C12 methyl ester fraction | MY | agg | Sphera |
C4 cut (butadiene) (approximation) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | ES | agg | Sphera |
C4 cut (butadiene) (approximation) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | CN | agg | Sphera |
C4 cut (butadiene) (approximation) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | JP | agg | Sphera |
C4 cut from FCC at refinery from crude oil ; production mix, at refinery ; 45.51 MJ/kg net calorific value | DE | agg | Sphera |
C4-cut (butadiene) steam cracker, from naphtha ; single route, at plant ; 45.3 MJ net calorific value | NL | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | DE | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | GB | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | IT | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | FR | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | EU-28 | agg | Sphera |
C4-raffinate by-product 1,3-butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; C4 hydrocarbons such as butadiene | NO | agg | Sphera |
C5 Hydrocarbon Resin Oil from C5 stream separation ; single route, at plant ; mainly contains pentadienes and cyclopentene | EU-28 | agg | Sphera |
C-6 fluorinated acrylic copolymer Esterification of 2-(Perfluorohexyl)ethanol by acrylic acid ; single route, at producer ; MW=418.15 g/mol | US | agg | Sphera |
Cable 10-core data ribbon 28AWG PE (25 g/m) 12.7x0.9 technology mix ; production mix, at plant ; tinned Cu wire, PE insulation, unshielded | GLO | agg | Sphera |
Cable 10-core data ribbon 28AWG PVC (25 g/m) 12.7x0.9 technology mix ; production mix, at plant ; tinned Cu wire, PVC insulation, unshielded | GLO | agg | Sphera |
Cable 1-core power 18AWG mPPE (10 g/m) D1.7 technology mix ; production mix, at plant ; tinned Cu wire, mPPE insulation | GLO | agg | Sphera |
Cable 1-core power 18AWG PE (16 g/m) D2.8 technology mix ; production mix, at plant ; tinned Cu wire, PE insulation | GLO | agg | Sphera |
Cable 1-core power 18AWG PTFE (13 g/m) D1.7 technology mix ; production mix, at plant ; tinned Cu wire, PTFE insulation | GLO | agg | Sphera |
Cable Ethernet Cat-6 PE/PVC (66 g/m) D6.4 technology mix ; production mix, at plant ; bare Cu wire, PE insulation, PVC jacket, unshi... | GLO | agg | Sphera |
Cable HDMI v1.0-1.3 28AWG PE/PVC (80 g/m) D7.3 technology mix ; production mix, at plant ; tinned Cu wire, PE insulation, PVC jacket, shi... | GLO | agg | Sphera |
Cadmium acetate (approximation) reaction of cadmium oxide with acetic acid ; single route, at plant ; 2.34 g/cm3, 230.50 g/mol | US | agg | Sphera |
Calcined kaolin powder (Al2O3 * SiO2) calcination in rotary furnace ; single route, at plant ; 162.06 g/mol | DE | agg | Sphera |
Calcined petroleum coke calcination ; single route, at plant ; 95 to 99 wt% carbon content | CN | agg | Sphera |
Calcium carbide from coke - flaring of CO rich gas reaction of calcium oxide with coke ; single route, at plant ; 2.22 g/cm3, 64.10 g/mol | DE | agg | Sphera |
Calcium carbide from coke - flaring of CO rich gas reaction of calcium oxide with coke ; single route, at plant ; 2.22 g/cm3, 64.10 g/mol | CN | agg | Sphera |
Calcium carbide from coke - flaring of CO rich gas reaction of calcium oxide with coke ; single route, at plant ; 2.22 g/cm3, 64.10 g/mol | US | agg | Sphera |
Calcium chloride (by-product epichlorohydrine, hydrochloric acid) from Epichlorhydrin synthesis, by-product epichlorohydrine, hydrochloric acid ; single route, at plant ; 110.98 g/mol | DE | agg | Sphera |
Calcium chloride 50% (CaCl2-6H2O) approximation produced from brine evaporation ; single route, at producer ; 50% H2O content | US | agg | Sphera |
Calcium chloride 75% (CaCl2-2H2O), from brine (approximation) produced from brine evaporation ; single route, at producer ; 22% H2O content | US | agg | Sphera |
Calcium chloride anhydrous (CaCl2-0H2O), from brine (approximation) produced from brine evaporation ; single route, at producer ; 0% H2O content | US | agg | Sphera |
Calcium chloride, by-product epichlorohydrine, hydrochloric acid from Epichlorhydrin synthesis, by-product epichlorohydrine, hydrochloric acid ; single route, at plant ; 110.98 g/mol | US | agg | Sphera |
Calcium chloride, by-product hydrochloric acid (100%) by-product epichlorohydrine via allyl chloride ; single route, at plant ; 2.15 g/cm3, 110.98 g/mol | EU-28 | agg | Sphera |
Calcium Cyanamide from calcium carbide and nitrogen ; production mix, at plant ; 2.29 g/cm3, 80.10 g/mol | CN | agg | Sphera |
Calcium Cyanamide from calcium carbide and nitrogen ; production mix, at plant ; 2.29 g/cm3, 80.10 g/mol | DE | agg | Sphera |
Calcium diformate (approximation) reaction of finelime and formaldehyde ; single route, at plant ; stoichiometrical approximation, density 2,02 g·c... | DE | agg | Sphera |
Calcium diformate (approximation) reaction of finelime and formaldehyde ; single route, at plant ; stoichiometrical approximation, density 2,02 g·c... | EU-28 | agg | Sphera |
Calcium hydroxide (Ca(OH)2; dry; slaked lime) lime slaking and distribution ; production mix, at plant ; 2.21 g/cm3, 74.10 g/mol | EU-28 | agg | Sphera |
Calcium hydroxide (Ca(OH)2; dry; slaked lime) lime slaking and distribution ; production mix, at plant ; 2.21 g/cm3, 74.10 g/mol | NL | agg | Sphera |
Calcium hydroxide (Ca(OH)2; dry; slaked lime) lime slaking and distribution ; production mix, at plant ; 2.21 g/cm3, 74.10 g/mol | US | agg | Sphera |
Calcium hydroxide (Ca(OH)2; dry; slaked lime) lime slaking and distribution ; production mix, at plant ; 2.21 g/cm3, 74.10 g/mol | UA | agg | Sphera |
Calcium hydroxide (Ca(OH)2; dry; slaked lime) lime slaking and distribution ; production mix, at plant ; 2.21 g/cm3, 74.10 g/mol | CN | agg | Sphera |
Calcium nitrate reaction of limestone and nitric acid ; single route, at plant ; 2.50 g/cm3, 164.08 g/mol | DE | agg | Sphera |
Calcium nitrate reaction of limestone and nitric acid ; single route, at plant ; 2.50 g/cm3, 164.08 g/mol | EU-28 | agg | Sphera |
Calcium stearate (stabilizer) reaction of stearic acid and caustic potash ; production mix, at plant ; 41.07 g/cm3, 607.04 g/mol | EU-28 | agg | Sphera |
Calcium sulfoaluminate cement (CSA) from alumina, gypsum and limestone via furnace process ; single route, at producer ; CSA cement requires kiln temperatures of arou... | US | agg | Sphera |
Calcium sulphate technology mix ; production mix, at plant ; 50% alpha hemihydrate, 50% beta hemihydrate | DE | agg | Sphera |
Calcium sulphate technology mix ; production mix, at plant ; 50% alpha hemihydrate, 50% beta hemihydrate | EU-28 | agg | Sphera |
Canola (rapeseed) meal (economic allocation) canola cultivation, transport, rape processing, pressing and extraction ; single route, at plant ; 49% dry carbon, 7% water content | US | agg | Sphera |
Caprolactam from Cyclohexanone from Cyclohexane (by-product ammonium sulphate) from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | BR | agg | Sphera |
Caprolactam from Cyclohexanone from Cyclohexane (by-product ammonium sulphate) from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | IN | agg | Sphera |
Caprolactam from Cyclohexanone from Cyclohexane (by-product ammonium sulphate) from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | EU-28 | agg | Sphera |
Caprolactam from Cyclohexanone from Cyclohexane (by-product ammonium sulphate) from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | BE | agg | Sphera |
Caprolactam from Cyclohexanone from Cyclohexane (by-product ammonium sulphate) from Cyclohexanone from Cyclohexane ; single route, at plant ; 1.01 g/cm3, 113 g/mol | CN | agg | Sphera |
Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | CN | agg | Sphera |
Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | EU-28 | agg | Sphera |
Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | FR | agg | Sphera |
Caprolactam from Cyclohexanone from Phenol from Cyclohexanone from Phenol ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | BE | agg | Sphera |
Caprolactam mix technology mix ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | EU-28 | agg | Sphera |
Caprolactam mix technology mix ; production mix, at plant ; 1.01 g/cm3, 113 g/mol | CN | agg | Sphera |
Caprolactone oxidation of cyclohenanone with peracetic acid ; production mix, at plant ; 1.03 g/cm3, 114.14 g/mol | US | agg | Sphera |
Caprylic Acid (Octanoic Acid) Enzymatic hydrolysis of palm oil, separation of capric acid ; single route, at plant ; 0.910 g/cm3, 144.21 g/mol | EU-28 | agg | Sphera |
Carbamate Mix technology mix ; production mix, at plant ; mix of carbamate 1 and carbamate 2 | DE | agg | Sphera |
Carbon dioxide (CO2) by-product ammonia (NH3) (economic allocation) Haber-Bosch process, from natural gas ; single route, at plant ; 1.98 kg/m3, 44.01 g/mol | JP | agg | Sphera |
Carbon dioxide (CO2) by-product ammonia (NH3) (economic allocation) Haber-Bosch process, from natural gas ; single route, at plant ; 1.98 kg/m3, 44.01 g/mol | EU-28 | agg | Sphera |
Carbon dioxide (CO2) by-product ammonia (NH3) (economic allocation) from ammonia synthesis, NH3/CO2 ; production mix, at producer ; 1.977 kg/m3, 44 g/mol | CN | agg | Sphera |
Carbon dioxide (CO2) by-product ammonia (NH3) (economic allocation) Haber-Bosch process, from natural gas ; single route, at plant ; 1.98 kg/m3, 44.01 g/mol | MY | agg | Sphera |
Carbon dioxide highly pure dewatering, trace removal ; single route, at plant ; 1,98 kg/m3, 44 g/mol | DE | agg | Sphera |
Carbon Fiber (CF; from PAN; standard strength) spinning, stabilizing, carbonizing, surface treatment, sizing ; production mix, at plant ; from PAN, standards strengths 34 million psi t... | EU-28 | agg | Sphera |
Carbon Fiber Reinforced Plastic (PF) from phenol formaldehyde resin and carbon fiber ; single route, at plant ; 60% phenol formaldehyde resin (PF), 40% carbon f... | DE | agg | Sphera |
Carbon fiber yarn (CF; from PAN; high strength) spinning, stabilizing, carbonizing, surface treatment, sizing ; single producer, at plant ; from PAN, high strengths 50 million psi tensi... | DE | agg | Sphera |
Carbon fiber yarn (CF; from PAN; intermediate strength) spinning, stabilizing, carbonizing, surface treatment, sizing ; single producer, at plant ; from PAN, intermediate strengths 42 million p... | DE | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | IT | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) via RER synthesis gas, from Iraqi natural gas ; single producer, at plant ; 1.25 kg/m3, 28.01 g/mol | NL | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | EU-28 | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | MY | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | GB | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | NL | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen) gasification of natural gas, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | CN | agg | Sphera |
Carbon monoxide via synthesis gas (coal based Syngas) gasification of coal, cryogenic separation of carbon monoxide and hydrogen ; single route, at plant ; 1.25 kg/m3, 28.01 g/mol | CN | agg | Sphera |
Cargo hauled by freight diesel train diesel driven, cargo ; consumption mix, to consumer ; average train, gross tonne weight 1000t, 7... | EU-28 | agg | Sphera |
Cargo hauled by freight electric train electricity driven, cargo ; consumption mix, to consumer ; average train, gross tonne weight 1000t, 7... | EU-28 | agg | Sphera |
Cargo hauled by truck trailer, 22 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck trailer, 22 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck trailer, 22 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck, 11.4 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 11.4 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 11.4 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 17.3 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 17.3 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 17.3 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 22 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck, 22 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck, 22 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Cargo hauled by truck, 24.7 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Cargo hauled by truck, 24.7 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Cargo hauled by truck, 24.7 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Cargo hauled by truck, 3.3 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Cargo hauled by truck, 3.3 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Cargo hauled by truck, 3.3 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Cargo hauled by truck, 5 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 5 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 5 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Cargo hauled by truck, 9.3 t payload [tkm] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Cargo hauled by truck, 9.3 t payload [tkm] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Cargo hauled by truck, 9.3 t payload [tkm] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Casein glue (PVAC dispersion) polymerization of vinyl acetate, PVAC dispersion in water ; single route, at plant ; 50% FKA | DE | agg | Sphera |
Cashew nut shell liquid (mass allocation) Cashew cultivation, sun drying, transport, cleaning and soaking, roasting ; single route, at plant ; 70% anacardic acids, 18% cardol, 5% cardanol; 76... | IN | agg | Sphera |
Cassava dry chips (mechanical chopping and sun drying) mechanical chopping and sun-drying ; single route, at producer ; 10% H2O | TH | agg | Sphera |
Castor oil - average, 50:50 mix of best case and worst case scenario castor oil pressing ; single route, at plant ; 72,5% carbon content | IN | agg | Sphera |
Castor oil - best case scenario castor oil pressing ; single route, at plant ; 72,5% carbon content | IN | agg | Sphera |
Castor oil - worst case scenario castor oil pressing ; single route, at plant ; 72,5% carbon content | IN | agg | Sphera |
Castor seed (8% H2O content) cultivation technology mix ; production mix, at field border ; 8% H2O | IN | agg | Sphera |
Catalyst (Vanadium pentoxide, sodium nitrate) components mixing, extruding, baking ; production mix, at plant ; 4 – 9 wt % vanadium pentoxide | DE | agg | Sphera |
Cattle hide, fresh (beef cattle, from slaughterhouse, economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Cattle hide, fresh (from slaughterhouse, economic allocation) - open input cattle raising slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | p-agg | Sphera |
Cattle hide, fresh (from slaughterhouse, economic allocation) - open input cattle raising slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | DE | p-agg | Sphera |
Cedar log free forest track (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 650 kg/m3, 0 % moisture content / 0 % H2O cont... | DE | agg | Sphera |
Cellulose based on timber spruce ; production mix, at plant ; 1.5 g/cm3 | US | agg | Sphera |
Cellulose (approximation, based on US foreground system) based on timber spruce ; production mix, at plant ; 44% carbon content | DE | agg | Sphera |
Cellulose acetate butyrate (approximation) viscose process ; single route, at plant ; 1.18 g/cm3 | DE | agg | Sphera |
Cement (CEM I 42.5) Portland cement technology mix ; production mix, at plant ; CEM I 42.5 | AE | agg | Sphera |
Cement (CEM IV 42.5) (economically allocated binders) technology mix ; production mix, at plant ; CEM IV | UA | agg | Sphera |
Cement average grinding - open input cement clinker materials grinding at grinding plant ; single route at plant ; 3000 kg/m3 | DE | p-agg | Sphera |
Ceramic (Passive components) including slurry preparation, shaping and burning ; single route, at plant ; Al2O3, silica sand, MnO2 mixture | GLO | agg | Sphera |
Cerium oxide primary production, ore mining and processing, electrolysis ; single route, at plant ; 6.77 g/cm3, 140.12 g/mol, RE95% | US | agg | Sphera |
Cerium oxide mix Rare earth element mining and processing ; single producer, at plant ; 85% China (Inner Mongolia Bayun Obo), 15% US... | GLO | agg | Sphera |
Cetyl Palmitate Esterification of Palmitic acid and Cetyl alcohol ; single route, at producer ; 0.82 g/cm3, 480.87 g/mol | DE | agg | Sphera |
Chlorinated Paraffins (approximation) reaction of paraffins with chlorine ; production mix, at plant ; 1.10- 1.26 g/cm3 | DE | agg | Sphera |
Chlorinated Polyethylene (approximation) reaction of polyethylene with chlorine ; production mix, at plant ; 1.27- 1.37 g/cm3 | DE | agg | Sphera |
Chlorine acetic acid (approximation) chlorination of acetic acid ; single route, at plant ; 1.58 g/cm3, 94.50 g·mol−1 | US | agg | Sphera |
Chlorine dioxide (1% ClO, 99% H2O; chlorate based process; SVP-LITE) (approximation) reduction of sodium chlorate with methanol ; single route, at plant ; 2.76 kg/m3, 67.45 g/mol | EU-28 | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm ; single route, at plant ; 3.2 g/l, 70.9 g/mol | CN | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm ; single route, at plant ; 3.2 g/l, 70.9 g/mol | AU | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm ; single route, at plant ; 3.2 g/l, 70.9 g/mol | PL | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | CH | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | SK | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | EU-28 | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | AU | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | HU | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | NO | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | GR | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | JP | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | NL | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | SE | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | IE | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) from chlorine-alkali electrolysis (membrane), from sodium chloride ; single route, at plant ; 35 g/mol | RU | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | PL | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | ES | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | AT | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) from chlorine-alkali electrolysis (membrane), from sodium chloride ; single route, at plant ; 35 g/mol | CN | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | GB | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | IN | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | CZ | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | PT | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | ES | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | FI | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | SI | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane ; single route, at plant ; 3.2 g/l, 70.9 g/mol | RO | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane) (open input energy, mass allocation) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 3.2 g/l, 70.9 g/mol | EU-28 | p-agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | PT | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | HU | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | EU-28 | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | RO | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | CZ | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | JP | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | PL | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | AU | agg | Sphera |
Chlorine mix technology mix ; production mix, at plant ; 3.2 kg/m3, 70.9 g/mol | SE | agg | Sphera |
Chloroacetic acid (approximation) chlorination of acetic acid ; single route, at plant ; 1.58 g/cm3, 94.50 g·mol−1 | DE | agg | Sphera |
Chloroacetyl chloride from chlorine acetyl acid reaction of chloroacetic acid with phosgene ; single route, at plant ; 1.42 g/cm3, 112.94 g/mol | DE | agg | Sphera |
Chloroacetylic acid from acetic acid chlorination of acetic acid ; single route, at plant ; 1.58 g/cm3, 94.50 g·mol−1 | DE | agg | Sphera |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene ; production mix, at plant ; 1.11 g/cm3, 112.56 g/mol | DE | agg | Sphera |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene ; production mix, at plant ; 1.11 g/cm3, 112.56 g/mol | EU-28 | agg | Sphera |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene ; production mix, at plant ; 1.11 g/cm3, 112.56 g/mol | JP | agg | Sphera |
Chlorobenzotrifluoride (p-) from chlorotoluene, chlorine and hydrogen fluoride ; production mix, at plant ; 180.55 g/mol | DE | agg | Sphera |
Chlorodifluoroethane (HCFC 142b) by-product Dichloro-1-fluoroethane (HCFC 141b) reaction of trichloroethane with hydrofluoric acid ; production mix, at plant ; 1.25 g/cm3, 116.94 g/mol | DE | agg | Sphera |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride ; production mix, at plant ; 3.94 kg/m3, 86.47 g/mol | GB | agg | Sphera |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride ; production mix, at plant ; 3.94 kg/m3, 86.47 g/mol | IT | agg | Sphera |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride ; single route, at plant ; 3.94 kg/m3, 86.47 g/mol | JP | agg | Sphera |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride ; production mix, at plant ; 3.94 kg/m3, 86.47 g/mol | EU-28 | agg | Sphera |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride ; production mix, at plant ; 3.94 kg/m3, 86.47 g/mol | NL | agg | Sphera |
Chloromethane/Methyl chloride hydrochlorination of methanol ; production mix, at plant ; 2.31 g/l, 50.49 g/mol | DE | agg | Sphera |
Chloromethane/Methyl chloride (HCl gas, boiling methanol, ZnCl2 catalyst) hydrochlorination of methanol ; production mix, at plant ; 2.31 g/l, 50.49 g/mol | DE | agg | Sphera |
Chloroprene (from butadiene via chlorination) from butadiene via chlorination ; single route, at plant ; 0.96 g/cm3, 88,54 g/mol | EU-28 | agg | Sphera |
Chloroprene (from butadiene via chlorination) from butadiene via chlorination ; single route, at plant ; 0.96 g/cm3, 88,54 g/mol | US | agg | Sphera |
Chloroprene (from butadiene via chlorination) from butadiene via chlorination ; single route, at plant ; 0.96 g/cm3, 88.54 g/mol | DE | agg | Sphera |
Chlorotoluene (p-chlorotoluene) chlorination of toluene ; single route, at plant ; 1.21 g/cm3, 140.57 g/mol | DE | agg | Sphera |
Chromated copper arsenate from chromic acid, copper sulphate and an arsenic compound ; single route, at plant ; consits of 34% arsenic compound | US | agg | Sphera |
Chromic acid from sodium dichromate ; production mix, at plant ; 1.20 g/cm3, 118 g/mol | DE | agg | Sphera |
Chromic acid anodizing - open input material to be anodised anodizing aluminium in chromic acid solution ; single producer, at plant ; 1 sqm coated | DE | p-agg | Sphera |
Citric acid (from starch) Enzymatic production of glucose, fermentation with aspergillus niger into citric acid ; single producer, at plant ; 1.665 g/cm3 anhydrous, 1.5g/cm3 monohydrate, ... | DE | agg | Sphera |
Citric acid (from starch) Enzymatic production of glucose, fermentation with aspergillus niger into citric acid ; single producer, at plant ; 1.665 g/cm3 anhydrous, 1.5g/cm3 monohydrate, ... | EU-28 | agg | Sphera |
Clay (21% H2O content) extraction and drying ; single route, at plant ; 21% water content | DE | agg | Sphera |
Clay (self-extraction) (average) Clay extraction ; single producer, at plant ; 17% moisture | DE | agg | Sphera |
Clay extracted from clay pit (23.7% moisture) technology mix ; production mix, at plant ; 23.7% moisture | EU-28 | agg | Sphera |
Clay extracted from clay pit (23.7% moisture) technology mix ; production mix, at plant ; 23.7% moisture | AT | agg | Sphera |
Clay powder, dried (mix) Clay mining, drying and processing ; production mix, at plant ; Clay from Pautzfeld and Tuningen | DE | agg | Sphera |
Clay production Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | DE | agg | Sphera |
Clay production Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | EU-28 | agg | Sphera |
Clay production Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | BR | agg | Sphera |
Clay production Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | CN | agg | Sphera |
Clay production Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | UA | agg | Sphera |
Clay production (approximation) Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | IN | agg | Sphera |
Clay production (refractory) open pit mining ; single producer, at plant ; crude clay | DE | agg | Sphera |
Clay production mix Clay extraction, mechanical processing and storage ; production mix, at plant ; 60% H2O content | DE | agg | Sphera |
Coal tar pitch (CTP) via distillation of coke-oven coal tar coke oven process ; single route, at plant ; 1.27–1.28 g/cm3 | DE | agg | Sphera |
Coarse colza meal (mass allocation) Preconditioning, pressing, extraction, refining, hexane combustion ; single route, at plant ; 53% carbon content, 19 MJ/kg net calorific value | DE | agg | Sphera |
Cobalt (only Cu/Co route) Copper cobalt route, hydrometallurgical process ; production mix, at plant ; 8.90 g/cm3, 58.93 g/mol | GLO | agg | Sphera |
Cobalt (only Ni/Co route) Nickel cobalt route, pyrometallurgical process ; single route, at plant ; 8.90 g/cm3, 58.93 g/mol, ferromagnetic | AU | agg | Sphera |
Cobalt (only Ni/Co route) Nickel cobalt route, pyrometallurgical process ; production mix, at plant ; 8.90 g/cm3, 58.93 g/mol | GLO | agg | Sphera |
Cobalt mix (Ni/Co and Cu/Co route) Nickel cobalt route, pyrometallurgical process and Copper cobalt route, hydrometallurgical process ; production mix, at plant ; 8.90 g/cm3, 58.93 g/mol | GLO | agg | Sphera |
Coconut cultivation - open input coconut husk technology mix ; production mix, at field border ; 48% H2O | PH | p-agg | Sphera |
Cocoyl chloride Chlorination of Stearic acid with Phosphorus trichloride ; single route, at plant ; molar mass: 289 g/mol, sum formula: C18H37Cl | EU-28 | agg | Sphera |
Coffee fruit (at field border, 50% H2O) Cultivation and harvesting ; single route, at farm ; 50% H2O | VN | agg | Sphera |
Coffee fruit (at field border, 50% H2O) (approximation) Cultivation and harvesting ; single route, at farm ; 50% H2O | BR | agg | Sphera |
Coking coal mix technology mix ; consumption mix, at border of producing ... ; 29 MJ/kg net calorific value | GLO | agg | Sphera |
Colemanite (extraction and processing) mining, cleaning, grinding, screening ; production mix, at plant ; 411.09 g/mol | DE | agg | Sphera |
Colemanite (extraction and processing) mining, cleaning, grinding, screening ; production mix, at plant ; 411.09 g/mol | US | agg | Sphera |
Colemanite (extraction and processing) mining, cleaning, grinding, screening ; production mix, at plant ; 411.09 g/mol | EU-28 | agg | Sphera |
Colemanite (extraction and processing) mining, cleaning, grinding, screening ; production mix, at plant ; 411.09 g/mol | CN | agg | Sphera |
Colophony (rosin) from tapped CN living pine, via gum rosin ; single route, at plant ; gum rosin | EU-28 | agg | Sphera |
Colophony (rosin) from tapped CN living pine, via gum rosin ; production mix, at plant ; gum rosin | CN | agg | Sphera |
Colophony (rosin) from distilled and esterified tall oil resin from distilled and esterified tall oil resin ; production mix, at plant ; gum rosin | FR | agg | Sphera |
Colophony (rosin, refined) from tapped CN living pine, via gum rosin, and from US pine stump, via wood rosin, technology mix ; consumption mix, at plant ; gum rosin | US | agg | Sphera |
Colophony (rosin, refined) from CN pine gum rosin from tapped CN living pine, via gum rosin ; production mix, at plant ; gum rosin | US | agg | Sphera |
Colophony (rosin, refined) from US pine stump from US pine stump ; consumption mix, at plant ; gum rosin | US | agg | Sphera |
Colophony / tall oil resin (approximation from paper production) separation from black liquor, depitching, fatty acid distillation ; single route, at plant ; gum rosin | US | agg | Sphera |
Colophony/tall oil resin (approximation from paper production) Kraft pulping, tall oil occurs as by-product ; single route, at plant ; composition: fatty acids about 42 to 55 %, resin... | SE | agg | Sphera |
Compressed air 1.5 bar (low power consumption) 1.5 bar, high efficiency ; consumption mix, at plant ; low electricity consumption | GLO | u-so | Sphera |
Compressed air 2 to 20 bar (high power consumption) 2 to 20 bar, low efficiency ; consumption mix, at plant ; high electricity consumption | GLO | u-so | Sphera |
Compressed air 2 to 20 bar (low power consumption) 2 to 20 bar, high efficiency ; consumption mix, at plant ; low electricity consumption | GLO | u-so | Sphera |
Compressed air 3.5 bar (low power consumption) 3.5 bar, high efficiency ; consumption mix, at plant ; low electricity consumption | GLO | u-so | Sphera |
Compressed natural gas (CNG) technology mix of screw-type and piston compressors ; production mix, at plant ; compression to 250 bar | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [CNG input in kg] Combustion of 1kg fuel input ; single route, at plant ; eta 1 | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [CNG input in kg] (direct) Combustion of 1kg fuel input ; single route, at plant ; eta 1, scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [CNG input in kg] (indirect) Combustion of 1kg fuel input ; single route, at plant ; eta 1, scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta] Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; eta 0,85 | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta] (direct) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; eta 0,85, scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Compressed natural gas (CNG) supplied and combusted [th. energy output in MJ, 85% eta] (indirect) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; eta 0,85, scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Concrete C20/25 mixing of cement, water and aggregates such as gravel ; production mix, at plant ; Compression strength class C20/25, CEM 1 32 us... | BR | agg | Sphera |
Concrete C20/25 mixing of cement, water and aggregates such as gravel ; production mix, at plant ; Compression strength class C20/25, CEM 1 32 us... | UA | agg | Sphera |
Concrete C30/37 mixing of cement, water and aggregates such as gravel ; production mix, at plant ; Compression strength class C20/25, CEM 1 32 us... | UA | agg | Sphera |
Concrete C30/37 mixing of cement, water and aggregates such as gravel ; production mix, at plant ; Compression strength class C20/25, CEM 1 32 us... | BR | agg | Sphera |
Concrete liquefier (ferrochrome-lignine sulfonate) technology mix ; production mix, at plant ; Ferrochrome-lignine sulfonate | EU-28 | agg | Sphera |
Condensed skim milk - open input steam thermal evaporation using steam heat ; production mix, at producer ; 65% H2O | US | p-agg | Sphera |
Connector audio TRS 2.5mm plug (2.0g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 2.5mm plug (2.0g) (gold-plated) | GLO | agg | Sphera |
Connector audio TRS 2.5mm plug (2.0g) (silver-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 2.5mm plug (2.0g) (silver-plated) | GLO | agg | Sphera |
Connector audio TRS 2.5mm socket (500mg) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 2.5mm socket (500mg) (gold-plated) | GLO | agg | Sphera |
Connector audio TRS 2.5mm socket (500mg) (silver-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 2.5mm socket (500mg) (silver-plated) | GLO | agg | Sphera |
Connector audio TRS 3.5mm plug (3.0g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 3.5mm plug (3.0g) (gold-plated) | GLO | agg | Sphera |
Connector audio TRS 3.5mm plug (3.0g) (nickel-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 3.5mm plug (3.0g) (nickel-plated) | GLO | agg | Sphera |
Connector audio TRS 3.5mm socket (800mg) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 3.5mm socket (800mg) (gold-plated) | GLO | agg | Sphera |
Connector audio TRS 3.5mm socket (800mg) (silver-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; 3.5mm socket (800mg) (silver-plated) | GLO | agg | Sphera |
Connector board-to-board 0.4mm-pitch SMD 60-pin plug (25mg) 15x2.6x1.0mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; board-to-board 0.4mm-pitch SMD 60-pin plug ... | GLO | agg | Sphera |
Connector board-to-board 0.4mm-pitch SMD 60-pin socket (56mg) 15x2.6x1.0mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; board-to-board 0.4mm-pitch SMD 60-pin socke... | GLO | agg | Sphera |
Connector China type I (38,7 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 38,7 g, 3 pins | GLO | agg | Sphera |
Connector Cinch female (15 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 15 g, 1 pin | GLO | agg | Sphera |
Connector Cinch female (15 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 15 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector Cinch male (4,1 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 4,1 g, 1 pin | GLO | agg | Sphera |
Connector Cinch male (4,1 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 4,1 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector coaxial micro-miniature W.FL SMD plug (18.6mg) 2.0x3.7x1.15mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; coaxial micro-miniature W.FL SMD plug (18.6... | GLO | agg | Sphera |
Connector coaxial micro-miniature W.FL SMD socket (5.6mg) 1.7x1.7x0.85mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; coaxial micro-miniature W.FL SMD socket (5.... | GLO | agg | Sphera |
Connector DC power female (2 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 1 pin | GLO | agg | Sphera |
Connector DC power male (2,9 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,9 g, 1 pin | GLO | agg | Sphera |
Connector D-Sub (20,4 g, 15 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 20,4 g, 15 pins, gold plated | GLO | agg | Sphera |
Connector D-Sub (21,1 g, 9 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 21,1 g, 9 pins, gold plated | GLO | agg | Sphera |
Connector D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold... | GLO | agg | Sphera |
Connector D-sub DE-15 (VGA) 15-pin socket (8.4g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; D-sub DE-15 (VGA) 15-pin socket (8.4g) (gol... | GLO | agg | Sphera |
Connector D-sub DE-9 (RS-232/serial) 9-pin plug (17.7g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; D-sub DE-9 (RS-232/serial) 9-pin plug (17.7... | GLO | agg | Sphera |
Connector D-sub DE-9 (RS-232/serial) 9-pin socket (7.2g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; D-sub DE-9 (RS-232/serial) 9-pin socket (7.... | GLO | agg | Sphera |
Connector HDMI type A (7,9 g, 19 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 7,9 g, 19 pins, gold plated | GLO | agg | Sphera |
Connector HDMI type D (2,7 g, 19 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,7 g, 19 pins, gold plated | GLO | agg | Sphera |
Connector HDMI Type-A 19-pin plug (7.8g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; HDMI Type-A 19-pin plug (7.8g) (gold-plated) | GLO | agg | Sphera |
Connector HDMI Type-A 19-pin socket (2.0g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; HDMI Type-A 19-pin socket (2.0g) (gold-plat... | GLO | agg | Sphera |
Connector HDMI Type-D 19-pin plug (2.7g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; HDMI Type-D 19-pin plug (2.7g) (gold-plated) | GLO | agg | Sphera |
Connector IC single-row (2 g, 10 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 10 pins | GLO | agg | Sphera |
Connector IC single-row (2 g, 10 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 10 pins, gold plated | GLO | agg | Sphera |
Connector IDC socket (5 g, 40 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 5 g, 40 pins, gold plated | GLO | agg | Sphera |
Connector IEC-60320-C13 female (28,5 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 28,5 g, 3 pins | GLO | agg | Sphera |
Connector IEC-60320-C14 male (9,1 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 9,1 g, 3 pins | GLO | agg | Sphera |
Connector IEC-60320-C5 female (16,8 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 16,8 g, 3 pins | GLO | agg | Sphera |
Connector IEC-60320-C6 male (5,5 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 5,5 g, 3 pins | GLO | agg | Sphera |
Connector IEC-60320-C7 female (5,5 g, 2 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 5,5 g, 2 pins | GLO | agg | Sphera |
Connector IEC-60320-C8 male (5 g, 2 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 5,5 g, 2 pins | GLO | agg | Sphera |
Connector Industries 230 V (120 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 120 g, 3 pins | GLO | agg | Sphera |
Connector Industries 400 V (180 g, 5 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 180 g, 5 pins | GLO | agg | Sphera |
Connector NEMA type A (19,2 g, 2 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 19,2 g, 2 pins | GLO | agg | Sphera |
Connector NEMA type B (27,7 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 27,7 g, 3 pins | GLO | agg | Sphera |
Connector PATA - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at plant ; 4 pins | GLO | agg | Sphera |
Connector PCI (2,6 g, 72 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,6 g, 72 pins, gold plated | GLO | agg | Sphera |
Connector power AC mains China Type-I 3-pin plug (38.7g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; China Type-I 3-pin plug (38.7g) | GLO | agg | Sphera |
Connector power AC mains Euro/Schuko Type-C CEE 7/16 2-pin plug (15g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; Euro/Schuko Type-C CEE 7/16 2-pin plug (15g) | GLO | agg | Sphera |
Connector power AC mains Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9... | GLO | agg | Sphera |
Connector power AC mains industrial 230V 3-pin plug (120g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; industrial 230V 3-pin plug (120g) | GLO | agg | Sphera |
Connector power AC mains industrial 400V 5-pin plug (180g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; industrial 400V 5-pin plug (180g) | GLO | agg | Sphera |
Connector power AC mains NEMA Type-A 2-pin plug (19.2g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; NEMA Type-A 2-pin plug (19.2g) | GLO | agg | Sphera |
Connector power AC mains NEMA Type-B 3-pin plug (27.7g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; NEMA Type-B 3-pin plug (27.7g) | GLO | agg | Sphera |
Connector power AC mains UK Type-G 3-pin plug (46.5g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; UK Type-G 3-pin plug (46.5g) | GLO | agg | Sphera |
Connector power DC circular plug (2.9g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; DC circular plug (2.9g) | GLO | agg | Sphera |
Connector power DC circular socket (2g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; DC circular socket (2g) | GLO | agg | Sphera |
Connector power IEC-60320-C13 3-pin plug (28.5g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C13 3-pin plug (28.5g) | GLO | agg | Sphera |
Connector power IEC-60320-C14 3-pin socket (10g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C14 3-pin socket (10g) | GLO | agg | Sphera |
Connector power IEC-60320-C5 3-pin plug (17.2g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C5 3-pin plug (17.2g) | GLO | agg | Sphera |
Connector power IEC-60320-C6 3-pin socket (5.5g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C6 3-pin socket (5.5g) | GLO | agg | Sphera |
Connector power IEC-60320-C7 2-pin plug (5.5g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C7 2-pin plug (5.5g) | GLO | agg | Sphera |
Connector power IEC-60320-C8 2-pin socket (5.0g) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; IEC-60320-C8 2-pin socket (5.0g) | GLO | agg | Sphera |
Connector RCA/Cinch plug (4.1g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; plug (4.1g) (gold-plated) | GLO | agg | Sphera |
Connector RCA/Cinch plug (4.1g) (silver-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; plug (4.1g) (silver-plated) | GLO | agg | Sphera |
Connector RCA/Cinch socket (2.9g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; socket (2.9g) (gold-plated) | GLO | agg | Sphera |
Connector RCA/Cinch socket (2.9g) (silver-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; socket (2.9g) (silver-plated) | GLO | agg | Sphera |
Connector RJ 45 (5,4 g, 8 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 5,4 g, 8 pins, gold plated | GLO | agg | Sphera |
Connector RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-... | GLO | agg | Sphera |
Connector RJ45/8P8C ethernet 8-pin socket (2.5g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; RJ45/8P8C ethernet 8-pin socket (2.5g) (gol... | GLO | agg | Sphera |
Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin plug (5.5g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; RJ45/8P8C ethernet EMI/RFI shielded 8-pin p... | GLO | agg | Sphera |
Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin socket (3.6g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; RJ45/8P8C ethernet EMI/RFI shielded 8-pin s... | GLO | agg | Sphera |
Connector S-ATA (2 g, 7 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 7 pins, gold plated | GLO | agg | Sphera |
Connector SATA 7 + 15 (22-pin) plug (1.4g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; SATA 7 + 15 (22-pin) plug (1.4g) (gold-plat... | GLO | agg | Sphera |
Connector SATA/SAS - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at plant ; 22 pins | GLO | agg | Sphera |
Connector Schuko CEE 7/7 (39,9 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 39,9 g, 3 pins | GLO | agg | Sphera |
Connector SD card micro THT/SMD socket (600mg) 14x16x1.7mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; SD card micro THT/SMD socket (600mg) 14x16x... | GLO | agg | Sphera |
Connector SIM card mini THT/SMD socket (1.1g) 26x18x1.8mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; SIM card mini THT/SMD socket (1.1g) 26x18x... | GLO | agg | Sphera |
Connector Steck Klemme Leiste (3 g, 2 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 3 g, 2 pins | GLO | agg | Sphera |
Connector Steck Rck Einpress Male (4,2 g, 55 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 4,2 g, 55 pins | GLO | agg | Sphera |
Connector TRS 2,5 female (10 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 10 g, 1 pin | GLO | agg | Sphera |
Connector TRS 2,5 female (10 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 10 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector TRS 2,5 male (2 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector TRS 2,5 male 2 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2 g, 1 pin | GLO | agg | Sphera |
Connector TRS 3,5 female (15 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 15 g, 1 pin | GLO | agg | Sphera |
Connector TRS 3,5 female (15 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 15 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector TRS 3,5 male (2,4 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,4 g, 1 pin | GLO | agg | Sphera |
Connector TRS 3,5 male (2,4 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,4 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector TRS 6,35 female (30 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 30 g, 1 pin | GLO | agg | Sphera |
Connector TRS 6,35 female (30 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 30 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector TRS 6,35 male (20 g, 1 pin) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 20 g, 1 pin | GLO | agg | Sphera |
Connector TRS 6,35 male (20 g, 1 pin, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 20 g, 1 pin, gold plated | GLO | agg | Sphera |
Connector UK type G (46,5 g, 3 pins) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 46,5 g, 3 pins | GLO | agg | Sphera |
Connector USB micro (2,5 g, 4 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,5 g, 4 pins, gold plated | GLO | agg | Sphera |
Connector USB micro Type-B 5-pin plug (2.5g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB micro Type-B 5-pin plug (2.5g) (gold-pl... | GLO | agg | Sphera |
Connector USB micro-AB THT/SMD 5-pin socket (260mg) 7.5x5.0x2.5mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB micro-AB THT/SMD 5-pin socket (260mg) 7... | GLO | agg | Sphera |
Connector USB mini (2,8 g, 4 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 2,8 g, 4 pins, gold plated | GLO | agg | Sphera |
Connector USB mini 5-pin socket (760mg) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB mini 5-pin socket (760mg) (gold-plated) | GLO | agg | Sphera |
Connector USB mini Type-B 5-pin plug (1.1g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB mini Type-B 5-pin plug (1.1g) (gold-pla... | GLO | agg | Sphera |
Connector USB type A (1,6 g, 4 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 1,6 g, 4 pins, gold plated | GLO | agg | Sphera |
Connector USB type B (8,1 g, 4 pins, gold plated) - based on parametric plan model technology mix; unit of reference flow in dataset is given in mass (kg) ; production mix, at producer ; 8,1 g, 4 pins, gold plated | GLO | agg | Sphera |
Connector USB Type-A 4-pin plug (9.2g) (gold-plated) 36x12x4.5mm technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB Type-A 4-pin plug (9.2g) (gold-plated) ... | GLO | agg | Sphera |
Connector USB Type-A 4-pin socket (2.1g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB Type-A 4-pin socket (2.1g) (gold-plated) | GLO | agg | Sphera |
Connector USB Type-B 4-pin plug (10.2g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB Type-B 4-pin plug (10.2g) (gold-plated) | GLO | agg | Sphera |
Connector USB Type-B 4-pin socket (2.8g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; USB Type-B 4-pin socket (2.8g) (gold-plated) | GLO | agg | Sphera |
Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; wire-to-board IDC 2.54mm-pitch 2x10 (20-pin... | GLO | agg | Sphera |
Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (tin-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; wire-to-board IDC 2.54mm-pitch 2x10 (20-pin... | GLO | agg | Sphera |
Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (gold-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; wire-to-board pin-header 2.54mm-pitch 2x10 ... | GLO | agg | Sphera |
Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (tin-plated) technology mix; unit of reference flow in dataset is 1 piece ; production mix, at producer ; wire-to-board pin-header 2.54mm-pitch 2x10 ... | GLO | agg | Sphera |
Copper chloride catalyst (approximation) direct combination of copper and chlorine ; single route, at plant ; 3.39 g/cm3, 134.45 g/mol | DE | agg | Sphera |
Copper chloride catalyst (approximation) direct combination of copper and chlorine ; single route, at plant ; 3.39 g/cm3, 134.45 g/mol | JP | agg | Sphera |
Copper phthalocyanine (approximation) phthalic anhydride- urea process ; single route, at plant ; 1.62 g/cm3, 576.07 g/mol | JP | agg | Sphera |
Copper phthalocyanine (approximation) phthalic anhydride- urea process ; single route, at plant ; 1.62 g/cm3, 576.07 g/mol | DE | agg | Sphera |
Copper sulphate as by-product from copper route mining, benefication, roasting, CuSO4 production ; production mix, at plant ; 3.60 g/cm3, 159.61 g/mol | US | agg | Sphera |
Copper sulphate as by-product from copper route mining, benefication, roasting, CuSO4 production ; production mix, at plant ; 3.60 g/cm3, 159.61 g/mol | CA | agg | Sphera |
Copper wire (0.06 mm) wire drawing ; single route, at plant ; 0.06mm | EU-28 | agg | Sphera |
Copper wire (0.06 mm) wire drawing ; single route, at plant ; 0.06mm | DE | agg | Sphera |
Copper wire (0.6 mm) wire drawing ; single route, at plant ; 0.6mm | EU-28 | agg | Sphera |
Cork (treated) Cork treatment ; single route, at plant ; 120–240 kg/m3 | DE | agg | Sphera |
Cork broken Cork treatment, cork breaking ; single route, at plant ; 120–240 kg/m3 | DE | agg | Sphera |
Cork flour Cork washing and grinding ; production mix, at plant ; grain size ~0,0001mm | DE | agg | Sphera |
Cork flour (EN15804 A1-A3) Cork washing and grinding ; production mix, at plant ; grain size ~0,0001mm | EU-28 | agg | Sphera |
Cork veneer Cork treatment ; single route, at plant ; 120–240 kg/m3 | DE | agg | Sphera |
Corn grain cultivation (35% H2O content) corn cultivation and harvesting ; production mix, at field border ; 35% H2O | CN | agg | Sphera |
Corrugated board 2018; 84,5% recycled fiber; cut-off EoL technology mix ; production mix, at producer ; 0,85 kg waste paper input per kg corrugated... | EU-28 | p-agg | Sphera/FEFCO |
Cotton fibre (conventional) cotton ginning ; single route, at plant ; length of fibers 0.5 inch to 2 inches,1.54–1.56 ... | US | agg | Sphera |
Cotton fibre (organic) cotton ginning ; single route, at plant ; length of fibers 0.5 inch to 2 inches,1.54–1.56 ... | US | agg | Sphera |
Cottonseed meal cotton cultivation, seed harvesting, pressing, extraction, refining ; single producer, at plant ; press cake from cotton oil pressing | US | agg | Sphera |
Cresol (p-cresol) sulfonation of toluene ; single route, at plant ; 1.05 g/cm3, 108.14 g/mol | DE | agg | Sphera |
Crude coconut oil harvest, pressing and extraction ; single route, at plant ; 80% carbon content | MY | agg | Sphera |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production ; consumption mix, to consumer ; 42.5 MJ/kg net calorific value | EU-28 | agg | Sphera |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production ; consumption mix, to consumer ; 42.4 MJ/kg net calorific value | KW | agg | Sphera |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production ; consumption mix, to consumer ; 42.2 MJ/kg net calorific value | RNA | agg | Sphera |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production ; consumption mix, to consumer ; 43.4 MJ/kg net calorific value | QA | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | SG | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | JP | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | KR | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | TH | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | TW | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | SA | agg | Sphera |
Cupric carbonate basic by-product sodium sulphate (approximation) reaction of copper sulphate and sodium carbonate ; production mix, at plant ; 4 g/cm3, 221 g/mol | EU-28 | agg | Sphera |
Cyanamide (50% solution) carbonation of calcium cyanamide ; production mix, at plant ; 1.28 g/cm3, 42.04 g/mol | CN | agg | Sphera |
Cyanamide (50% solution) carbonation of calcium cyanamide ; production mix, at plant ; 1.28 g/cm3, 42.04 g/mol | DE | agg | Sphera |
Cyanogen Chloride (via chlorination of hydrocyanic acid) chlorination of hydrocyanic acid ; single route, at plant ; 61.47 g/mol | DE | agg | Sphera |
Cyanuric acid pyrolysis of urea ; production mix, at plant ; 2.5 g/cm3, 129.07 g/mol | DE | agg | Sphera |
Cyanuric chloride (via trimerization of cyanogen chloride) via trimerization of cyanogen chloride ; single route, at plant ; 1.32 g/cm3, 184.40 g/mol | DE | agg | Sphera |
Cyclododecatriene (CDT, 1,5,9-Cyclododecatriene) cyclotrimerization of butadiene ; production mix, at plant ; 0.89 g/cm3, 162.28 g/mol | DE | agg | Sphera |
Cyclododecatriene by-products 1,5-Cyclooctadiene, 4-Vinylcyclohexene cyclotrimerization of butadiene ; single route, at plant ; 0.89 g/cm3, 162.28 g/mol | DE | agg | Sphera |
Cyclohexane catalytic hydration of benzene ; production mix, at plant ; 0.7781 g/mL, 84.16 g/mol | EU-28 | agg | Sphera |
Cyclohexane catalytic hydration of benzene ; production mix, at plant ; 0.7781 g/mL, 84 g/mol | BR | agg | Sphera |
Cyclohexanone from cyclohexane ; production mix, at plant ; 0.95 g/cm3, 98.15 g/mol | DE | agg | Sphera |
DDGS (from ethanol from corn) Corn dry mill process ; single producer, at plant ; 26.5% CP | US | agg | Sphera |
Decabromodiphenyl ethane (approximation) reaction of diphenyl ethane with bromine ; single route, at plant ; 971.22 g/mol | DE | agg | Sphera |
Decanoic acid (capric acid) from palm kernel oil (approximation) Enzymatic hydrolysis of palm oil, separation of capric acid ; single producer, at plant ; density: 0.893 g/cm3, molar mass: 172.26 g mo... | EU-28 | agg | Sphera |
Degreasing agent (aluminium) mixture of soda, tensides, isononanol and water ; production mix, at plant ; estimation, degreaser | DE | agg | Sphera |
Deionised water via ion exchange ; single route, at plant ; 1000 kg/m3, 18 g/mol | EG | agg | Sphera |
Deionised water via ion exchange ; single route, at plant ; 1000 kg/m3, 18 g/mol | GR | agg | Sphera |
Deionised water via ion exchange ; single route, at plant ; 1000 kg/m3, 18 g/mol | CH | agg | Sphera |
Deionised water (approximation) via ion exchange ; single route, at plant ; 1 kg/l, 18 g/mol | TH | agg | Sphera |
Deionised water (approximation) via ion exchange ; single route, at plant ; 1 kg/l, 18 g/mol | MY | agg | Sphera |
Deionised water (approximation) via ion exchange ; single route, at plant ; 1 kg/l, 18 g/mol | IN | agg | Sphera |
Deionised water (reverse-osmosis/electrical-deionisation) technology mix, reverse-osmosis/electrical-deionisation ; production mix, at plant ; 1000 kg/m3, 18 g/mol | JP | agg | Sphera |
Deionised water (reverse-osmosis/electrical-deionisation) technology mix, reverse-osmosis/electrical-deionisation ; production mix, at plant ; 1000 kg/m3, 18 g/mol | EU-28 | agg | Sphera |
Deionised water (reverse-osmosis/electrical-deionisation) technology mix, reverse-osmosis/electrical-deionisation ; production mix, at plant ; 1000 kg/m3, 18 g/mol | US | agg | Sphera |
Desalinated sea water (reverse osmosis with energy recovery) reverse osmosis with energy recovery ; single route, at plant ; 1000 kg/m3, 18 g/mol | DE | agg | Sphera |
Desalinated sea water (reverse osmosis without energy recovery) reverse osmosis without energy recovery ; single route, at plant ; 1000 kg/m3, 18 g/mol | DE | agg | Sphera |
Desalinated sea water (Vaporisation, MSF-Plant) vaporisation, multi- stage- flash plant ; single route, at plant ; 1000 kg/m3, 18 g/mol | DE | agg | Sphera |
Desalinated sea water technology mix technology mix, multi stage flash and reverse osmosis ; production mix, at plant ; 1000 kg/m3, 18 g/mol | DE | agg | Sphera |
Desalinated sea water technology mix (Abu Dhabi) technology mix, multi stage flash and reverse osmosis ; production mix, at plant ; 1000 kg/m3, 18 g/mol | AE | agg | Sphera |
Desalinated sea water technology mix (Dubai) technology mix, multi stage flash 95% and reverse osmosis 5% ; production mix, at plant ; 1000 kg/m3, 18 g/mol | AE | agg | Sphera |
Diammonium phosphate granular fertilizer (DAP) reaction of ammonia and phosphoric acid ; single producer, at plant ; density 1.619 g/cm3, molar mass 132.07 g/mol | DE | agg | Sphera |
Dibenzanthrone alkaline fusion of benzanthrone ; production mix, at plant ; 1.53 g/cm3, 456.49 g/mol | US | agg | Sphera |
Dibenzyl toluene (DBT) Friedel–Crafts reaction, from toluene and benzyl chloride ; single route, at producer ; 272.38 g/mol | DE | agg | Sphera |
Dichloromethane chlorination of methyl chloride ; production mix, at plant ; 1.33 g/cm3, 84.93 g/mol | EU-28 | agg | Sphera |
Dichloromethane (approximation) chlorination of methyl chloride ; production mix, at plant ; 1.33 g/cm3, 84.93 g/mol | US | agg | Sphera |
Dichloropropene by-product allyl chloride (C3H5Cl) chlorination of propene ; single route, at plant ; 1.16 g/cm3, 112.98 g/mol | DE | agg | Sphera |
Dichlorotetrafluoroethane (R114) (approximation) from perchloroethylene, hydrogen fluoride and chlorine ; production mix, at plant ; 1.46 g/cm3, 170.92 g/mol | DE | agg | Sphera |
Dichlorpropane by-product epichlorohydrin, hydrochloric acid chlorination of propene ; single route, at plant ; 1.16 g/cm3, 112.98 g/mol | DE | agg | Sphera |
Dicumyl peroxide (stoichiometric approximation) via cumyl hydroperoxide ; single route, at plant ; 1.02 g/cm3, 270.37 g/mol | EU-28 | agg | Sphera |
Dicyclopentadiene (from C5 stream separation) from C5 stream separation ; single route, at plant ; 0.978 g/cm3, 132.20 g/mol | EU-28 | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | DE | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 15 ppm sulphur | US | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | JP | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 500 ppm sulphur | BR | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 800 ppm sulphur | CN | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | FR | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | EU-28 | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | AU | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | NL | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 50 ppm sulphur | MY | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | GB | agg | Sphera |
Diesel at refinery from crude oil ; production mix, at refinery ; 350 ppm sulphur | IN | agg | Sphera |
Diesel at refinery Western Australia from crude oil ; production mix, at refinery ; 10 ppm sulphur | AU | agg | Sphera |
Diesel combustion forest engines diesel- driven forest engine ; single operation, at work station ; 1 kg diesel combusted | GLO | u-so | Sphera |
Diesel combustion in construction machine (18-36 kW; Stage IIIA) diesel driven ; consumption mix, to consumer ; 18-36 kW | GLO | u-so | Sphera |
Diesel Exhaust Fluid (DEF) mixing Stami Carbon urea with water ; production mix, at plant ; 68% urea, 32% water | EU-28 | agg | Sphera |
Diesel fuel supplied and combusted in diesel generator technology mix regarding firing and flue gas cleaning ; production mix, at diesel generator ; 85% CHP efficiency | EU-28 | agg | Sphera |
Diesel fuel supplied and combusted in diesel generator (direct) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 85% CHP efficiency | EU-28 | agg | Sphera |
Diesel fuel supplied and combusted in diesel generator (indirect) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 85% CHP efficiency | EU-28 | agg | Sphera |
Diesel generator mechanical diesel engine ; single operation, at work station ; >500 kW | GLO | u-so | Sphera |
Diesel mix at refinery from crude oil and bio components ; production mix, at refinery ; 10 ppm sulphur, 6.89 wt.% bio components; 5... | NL | agg | Sphera |
Diesel mix at refinery from crude oil and bio components ; production mix, at refinery ; 10 ppm sulphur, 10.57 wt.% bio components; ... | FR | agg | Sphera |
Diesel mix at refinery from crude oil and bio components ; production mix, at refinery ; 350 ppm sulphur, 0.00 wt.% bio components | RU | agg | Sphera |
Diesel mix at refinery from crude oil and bio components ; production mix, at refinery ; 50 ppm sulphur, 7.49 wt.% bio components; 5... | MY | agg | Sphera |
Diesel mix at refinery Western Australia from crude oil and bio components ; production mix, at refinery ; 10 ppm sulphur, 0.09 wt.% bio components; 0... | AU | agg | Sphera |
Diethanolamine (DEA) by-prod. ethanolamines Reaction of ethylene oxide with excess of ammonia ; production mix, at producer ; 100% active substance, 1.09 g/cm3, 105.14 g... | DE | agg | Sphera |
Diethyl carbonate (DEC) phosgenation of ethanol ; single producer, at plant ; 0.975 g/cm3, 118.13 g/mol | DE | agg | Sphera |
Diethyl ether from ethylene ; production mix, at plant ; by-product ethanol (96%) | DE | agg | Sphera |
Diethyl ether (approximation) from ethylene ; production mix, at plant ; by-product ethanol (96%) | CN | agg | Sphera |
Diethylamine (by-product Ethylamine, triethylamine (TEA) from ethanol and ammonia, by-product Ethylamine, Triethylamine ; production mix, at plant ; 0.70 g/cm3, 73.14 g/mol | DE | agg | Sphera |
Diethylaniline (2,6) from aniline reraction of ethene and aniline ; single route, at plant ; 0.93 g/cm3, 149.24 g/mol | DE | agg | Sphera |
Diethyldithiocarbamate from diethyl amine, sodium hydroxide and carbon disulphide ; production mix, at plant ; 1.1 g/cm3, 171.26 g/mol | DE | agg | Sphera |
Diethylene glycol by product ethylene glycol from ethene and oxygen via EO from ethene and oxygen ; single route, at plant ; 1.12 g/m³, 106 g/mol | EU-28 | agg | Sphera |
Diethylene glycol by product ethylene glycol from ethene and oxygen via EO from ethene and oxygen ; single route, at plant ; 1.12 g/m³, 106 g/mol | BE | agg | Sphera |
Diethylene glycol by product ethylene glycol from ethene and oxygen via EO (approximation) from ethene and oxygen ; single route, at plant ; 1.12 g/m³, 106 g/mol | SA | agg | Sphera |
Diethylenetriamine (DETA) reaction of ethylene dichloride and ammonia ; single route, at plant ; C4H13N3, CAS 111-40-0 | NL | agg | Sphera |
Dihydromyrcenol in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 28% of the energy output is el... | EU-28 | p-agg | Sphera |
Di-iso-butyl Aluminium Hydride (DiBaH) hydration and butylation of aluminium ; production mix, at plant ; 0.79 g/cm3, 142.22 g/mol | DE | agg | Sphera |
Di-isononyl phthalate (DINP / DOP) esterification of phthalic acid ; production mix, at plant ; 0.98 g/cm3, 418.62 g/mol | DE | agg | Sphera |
Di-isononyl phthalate (DINP) esterification of phthalic acid ; production mix, at plant ; 0.98 g/cm3, 418.62 g/mol | US | agg | Sphera |
Di-isopropanolamine (by-product MIPA, TIPA) reaction of propylene oxide and ammonia ; single route, at plant ; 0.99 g/cm3, 133.19 g/mol | DE | agg | Sphera |
Dimethyl adipate (Dimethyl adipic acid ester) transesterification of adipic acid with methanol ; single route, at plant ; 1.06 g/cm3, 174.19 g/mol | NL | agg | Sphera |
Dimethyl carbonate (DMC) gaseous phase; from methanol and carbon monoxide; by-product dimethyleneoxalate ; production mix, at plant ; 90.08 g/mol | DE | agg | Sphera |
Dimethyl succinate (approximation) cataltytic hydrogenation of maleic acid and the esterification of succinic acid with methanol ; single route, at plant ; 1.117 g/mL, 146.14 g/mol | DE | agg | Sphera |
Dimethyl sulfoxide (from Dimethyl sulphide) catalytic oxidation of dimethyl sulfide with oxygen ; single route, at plant ; 1.10 g/cm3, 78.13 g/mol | US | agg | Sphera |
Dimethyl sulfoxide (from Dimethylsulphide) catalytic oxidation of dimethyl sulfide with oxygen ; single route, at plant ; 1.10 g/cm3, 78.13 g/mol | DE | agg | Sphera |
Dimethyl terephthalate (DMT) oxidation of p-xylene ; production mix, at plant ; 1.35 g/cm3, 194.19 g/mol, 22.8 MJ/kg net calor... | EU-28 | agg | Sphera |
Dimethylamine by-product mono-, trimethyleneamine reaction of methanol and ammonia ; production mix, at plant ; 0.67 g/cm3, 45.08 g/mol | US | agg | Sphera |
Dimethylamine by-product mono-, trimethyleneamine reaction of methanol and ammonia ; production mix, at plant ; 0.67 g/cm3, 45.08 g/mol | DE | agg | Sphera |
Dimethylamine by-product mono-, trimethyleneamine reaction of methanol and ammonia ; production mix, at plant ; 0.67 g/cm3, 45.08 g/mol | EU-28 | agg | Sphera |
Dimethyldichlorosilane Rochow-Müller-process ; single route, at plant ; 1.06 g/cm3, 129.06 g/mol | US | agg | Sphera |
Dimethyldichlorosilane Rochow-Müller-process ; single route, at plant ; 1.06 g/cm3, 129.06 g/mol | EU-28 | agg | Sphera |
Dimethyldichlorosilane Rochow-Müller-process ; single route, at plant ; 1.06 g/cm3, 129.06 g/mol | DE | agg | Sphera |
Dimethylformamide (DMF) (approximation) catalyzed reaction of dimethylamine and carbon monoxide ; single route, at plant ; 0.948 g/cm3, 73.09 g/mol | DE | agg | Sphera |
Dimethyloxalate oxidative carbonylation of methanol ; single route, at plant ; 1.15 g/cm3, 118.09 g/mol | DE | agg | Sphera |
Dimethylsulphidetoluene diamine (DMTDA) (approximation) reaction of toluene diamine with an organic disulphide ; production mix, at plant ; 1.21 g/cm3, 214.36 g/mol | DE | agg | Sphera |
Di-n-butene via Octol Process industry mix, from n-butene ; single route, at plant ; 0.62 g/cm3, 56.11 g/mol | US | agg | Sphera |
Dinitromethane, potassium salt from 1,2,4-triazol-5-on, nitric acid (96%) and sulphuric acid (96%) ; single route, at plant ; 144 g/mol | EU-28 | agg | Sphera |
Dinitrotoluene nitration of toluene ; production mix, at plant ; 1.52 g/cm3, 182,14 g/mol | EU-28 | agg | Sphera |
Dinitrotoluene nitration of toluene ; production mix, at plant ; 1.52 g/cm3, 182,14 g/mol | CN | agg | Sphera |
Dioctyl phthalate/di-(2-ethylhexyl) phthalate (DOTP, DEHP) from transesterification of DMT transesterification of Dimethylterephthalate and octanol ; single route, at plant ; 0,98 g/cm3, 390.56 g/mol | US | agg | Sphera |
Dioctylphthalate/di (2-ethylhexyl) phthalate (DOP, DEHP) esterification of phthalic anhydride and octanol ; single route, at plant ; 0,98 g/cm3, 390.56 g/mol | EU-28 | agg | Sphera |
Dioctylphthalate/di-(2-ethylhexyl) phthalate (DOTP, DEHP) from esterification of phthalic anhydride esterification of phthalic anhydride and octanol ; single route, at plant ; 0,98 g/cm3, 390.56 g/mol | US | agg | Sphera |
Dioxothiolane (Sulfolan) from butadiene, via sulfolene ; production mix, at plant ; 1.26 g/cm3, 120.17 g/mol | DE | agg | Sphera |
Diphenyl (via benzene from toluene dealkylation) Byproduct of benzene process from toluene dealkylation ; production mix, at plant ; 1.04 g/cm3, 154.21 g/mol | DE | agg | Sphera |
Diphenyloxide (approximation) non-catalytic process for the production of diphenyloxid and phenylphenol ; production mix, at plant ; 170.21 g/mol | EU-28 | agg | Sphera |
Dipropylene glycol from propylene oxide, by product propylene glycol ; production mix, at plant ; 1.02 g/cm3, 134.17 g/mol | DE | agg | Sphera |
Dipropyleneglycol dibenzoate plast production from dipropylene glycol and methyl benzoate ; production mix, at plant ; 342.39 g/mol | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car >2 l biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car >2 l (direct) biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car >2 l (indirect) biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car 1,4-2 l biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car 1,4-2 l (direct) biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by biodiesel (B100) car 1,4-2 l (indirect) biodiesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.3 l CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,3l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.3 l (direct) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,3l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.3 l (indirect) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,3l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.6 l CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,6l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.6 l (direct) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,6l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.6 l (indirect) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,6l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.9 l CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,9l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.9 l (direct) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,9l | EU-28 | agg | Sphera |
Distance travelled by compressed natural gas (CNG) car 1.9 l (indirect) CNG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,9l | EU-28 | agg | Sphera |
Distance travelled by diesel car >2 l diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by diesel car >2 l (direct) diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by diesel car >2 l (indirect) diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by diesel car 1,4-2 l diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by diesel car 1,4-2 l (direct) diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by diesel car 1,4-2 l (indirect) diesel driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car <1,4 l gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by gasoline car <1,4 l (direct) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by gasoline car <1,4 l (indirect) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by gasoline car >2 l gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car >2 l (direct) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car >2 l (indirect) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size more than 2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car 1,4-2 l gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car 1,4-2 l (direct) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by gasoline car 1,4-2 l (indirect) gasoline driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by IC/ EC train electricity driven, passenger train ; consumption mix, to consumer ; IC/EC train | DE | agg | Sphera |
Distance travelled by ICE train <200 kmh electricity driven, passenger train ; consumption mix, to consumer ; ICE train <200 kmh | DE | agg | Sphera |
Distance travelled by ICE train >200 kmh electricity driven, passenger train ; consumption mix, to consumer ; ICE train >200 kmh | DE | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l (direct) LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l (indirect) LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size up to 1,4l | EU-28 | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (direct) LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (indirect) LPG driven, Euro 4, passenger car ; consumption mix, to consumer ; engine size 1,4-2l | EU-28 | agg | Sphera |
Distance travelled by plane (1000 km) technology mix, kerosene driven, passenger plane ; production mix, at plant ; 1000 km | EU-28 | agg | Sphera |
Distance travelled by plane (250 km) technology mix, kerosene driven, passenger plane ; production mix, at plant ; 250 km | EU-28 | agg | Sphera |
Distance travelled by plane (500 km) technology mix, kerosene driven, passenger plane ; production mix, at plant ; 500 km | EU-28 | agg | Sphera |
Distance travelled by plane (5000 km) technology mix, kerosene driven, passenger plane ; production mix, at plant ; 5000 km | EU-28 | agg | Sphera |
Distance travelled by RE/ RB/ IRE train electricity driven, passenger train ; consumption mix, to consumer ; RE/ RB/ IRE train | DE | agg | Sphera |
Distance travelled by truck trailer, 22 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck trailer, 22 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck trailer, 22 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 34t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck, 11.4 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 11.4 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 11.4 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 14 - 20t gross weight, 11,4t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 17.3 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 17.3 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 17.3 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 20 - 26t gross weight, 17,3t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 22 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck, 22 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck, 22 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 28 - 32t gross weight, 22t payload... | EU-28 | agg | Sphera |
Distance travelled by truck, 24.7 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Distance travelled by truck, 24.7 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Distance travelled by truck, 24.7 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, more than 32t gross weight, 24,7t ... | EU-28 | agg | Sphera |
Distance travelled by truck, 3.3 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Distance travelled by truck, 3.3 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Distance travelled by truck, 3.3 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, up to 7,5t gross weight, 3,3t payl... | EU-28 | agg | Sphera |
Distance travelled by truck, 5 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 5 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 5 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 7,5 t - 12t gross weight, 5t paylo... | EU-28 | agg | Sphera |
Distance travelled by truck, 9.3 t payload [km] diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Distance travelled by truck, 9.3 t payload [km] (direct) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Distance travelled by truck, 9.3 t payload [km] (indirect) diesel driven, cargo ; consumption mix, to consumer ; Euro 4, 12-14t gross weight, 9,3t payload ... | EU-28 | agg | Sphera |
Distance travelled by urban railway electricity driven, passenger train ; consumption mix, to consumer ; passenger train urban | DE | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | Sphera |
District cooling (approximation) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ES | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PT | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | DE | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AE | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NL | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CA | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CZ | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FR | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GR | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PL | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SE | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | BE | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | LU | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CH | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | HU | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NO | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FI | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AT | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GB | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | JP | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MX | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SG | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MY | agg | Sphera |
District cooling (approximation) (direct) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | US | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GR | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SE | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | JP | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ES | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | DE | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NL | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GB | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | US | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PL | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AT | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MX | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AE | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | HU | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SG | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | BE | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MY | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | LU | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FR | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FI | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NO | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CA | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CH | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PT | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | Sphera |
District cooling (approximation) (indirect) pumping cold water, electricity needed for powering pumps ; production mix, at plant ; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CZ | agg | Sphera |
District heating mix technology mix ; production mix, at plant ; 10.7 % energy loss during transmission | CN | agg | Sphera |
District heating mix technology mix ; production mix, at plant ; 10.7 % energy loss during transmission | DE | agg | Sphera |
Dodecanoic acid (Lauric acid) from refined palm oil ; single route, at plant ; 1.01 g/cm3, 200.32 g/mol | DE | agg | Sphera |
Dolomite (ground) dolomite mining and milling ; single route, at plant ; 2.90 g/cm3 | DE | agg | Sphera |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite ; production mix, at plant ; 2.90 g/cm3 | EU-28 | agg | Sphera |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite ; production mix, at plant ; 2.90 g/cm3 | US | agg | Sphera |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite ; production mix, at plant ; 2.90 g/cm3 | DE | agg | Sphera |
Dolomite mining dolomite mining ; single route, at plant ; 2.90 g/cm3 | DE | agg | Sphera |
Dolomite mining dolomite mining ; single route, at plant ; 2.90 g/cm3 | EU-28 | agg | Sphera |
Dolomite mining dolomite mining ; single route, at plant ; 2.90 g/cm3 | US | agg | Sphera |
Dolomite mining open pit mining and processing ; production mix, at plant ; 2.90 g/cm3 | CN | agg | Sphera |
Domestic waste (wood, natural finish) on landfill landfill including landfill gas utilisation and leachate treatment and without collection, transport and pre-treatment ; production mix (region specific sites), ... ; wood, natural finish | EU-28 | p-agg | Sphera |
Dragon seed (lat. Lallemantia iberica) dried (9% H2O content) Dragon seed cultivation (seeding technique, fertilizing, using pesticides), harvesting, drying ; single route, at field border ; 9% H2O (maximum moisture for storage) | DE | agg | Sphera |
Dried quartz sand (grain size 0/2) technology mix ; production mix, at plant ; grain size 0/2 | EU-28 | agg | Sphera |
Dried starch (corn wet mill), economic allocation corn wet milling, starch washing and drying ; single producer, at plant ; dried starch | CN | agg | Sphera |
Dried starch (Polyglucose) from corn (economic allocation) corn cultivation and harvesting, wet milling process ; single producer, at plant ; dried corn starch | EU-28 | agg | Sphera |
Dry haricot beans (14% H2O) bean cultivation and harvest ; production mix, at field border ; 14 % H2O | US | agg | Sphera |
Dyes mixture of aniline and 2,4-dimethylbenzaldehyde ; single producer, at plant ; 50% aniline, 50% dimethylbenzaldehyde | DE | agg | Sphera |
Dysprosium (price allocated) primary production, ore mining and processing, electrolysis ; production mix, at plant ; 8.56 g/cm3, 162.50 g/mol | CN | agg | Sphera |
Dysprosium Production (mass allocated) mining and processing, primary production ; production mix, at plant ; 8.54 g/cm3, 162.50 g/cm3 | CN | agg | Sphera |
EAF high speed steel (HSS-6-5-2) electric arc furnace route ; production mix, at plant ; 1 kg | DE | p-agg | Sphera |
EAF Steel billet / slab / bloom EAF route ; production mix, at plant ; Crude steel | EU-28 | p-agg | Sphera |
Electricity from biogas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from biogas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | TH | agg | Sphera |
Electricity from biogas (direct) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from biogas (indirect) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from biomass (solid) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | KE | agg | Sphera |
Electricity from biomass (solid) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | CL | agg | Sphera |
Electricity from biomass (solid) (direct) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from biomass (solid) (indirect) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from coal gases AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from diesel fuel (diesel generator) technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 85% CHP efficiency | EU-28 | agg | Sphera |
Electricity from diesel fuel (diesel generator) (direct) technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 85% CHP efficiency | EU-28 | agg | Sphera |
Electricity from diesel fuel (diesel generator) (indirect) technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 85% CHP efficency | EU-28 | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | RO | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | AT | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | IS | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | NO | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | GB | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | SK | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | FI | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | DK | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | LT | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | CH | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | CZ | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | HU | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | BG | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | IT | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | MT | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | SI | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | GR | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | NL | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | EE | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | PT | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | IE | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | SE | agg | Sphera |
Electricity from fossil unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | HR | agg | Sphera |
Electricity from hard coal AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | MA | agg | Sphera |
Electricity from hard coal AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | CL | agg | Sphera |
Electricity from hard coal AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | PH | agg | Sphera |
Electricity from heavy fuel oil (HFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | KW | agg | Sphera |
Electricity from heavy fuel oil (HFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | PK | agg | Sphera |
Electricity from heavy fuel oil (HFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from heavy fuel oil (HFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | KE | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | IQ | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | BA | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | PY | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | IS | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | PK | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | EG | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | KZ | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | CO | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | TW | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | UA | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | HR | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | AR | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | KH | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | TH | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | PA | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | SV | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | KR | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | PH | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | CL | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | HN | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | MX | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | NI | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | LK | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | MA | agg | Sphera |
Electricity from hydro power AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | NG | agg | Sphera |
Electricity from hydro power (direct) AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from hydro power (indirect) AC, technology mix of run-off-river, storage and pump storage ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from light fuel oil (LFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from light fuel oil (LFO) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | FR | agg | Sphera |
Electricity from lignite AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | PK | agg | Sphera |
Electricity from natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | AE | agg | Sphera |
Electricity from natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | QA | agg | Sphera |
Electricity from natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | IL | agg | Sphera |
Electricity from natural gas - open input natural gas AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | US | p-agg | Sphera |
Electricity from natural gas (direct) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from natural gas (indirect) AC, mix of direct and CHP, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from natural gas via CHP (without supply) - open input natural gas AC, combined heat and power generation (CHP), technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | US | p-agg | Sphera |
Electricity from natural gas via direct (without supply) - open input natural gas AC, direct combustion, technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; 1kV - 60kV | US | p-agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | LK | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | IQ | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | PE | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | HK | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | OM | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at producer ; 1kV - 60kV | DZ | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | BA | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | GLO | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | IS | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | SV | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | IL | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | PA | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | AR | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | HR | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | PH | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | EE | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | KZ | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | KW | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | AE | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | MM | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | KH | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at producer ; 1kV - 60kV | EG | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | KE | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | MA | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | MK | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at producer ; 1kV - 60kV | UA | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | NG | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | VE | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | TW | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | CL | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | BD | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | HN | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | NI | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | SA | agg | Sphera |
Electricity from photovoltaic AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | PK | agg | Sphera |
Electricity from photovoltaic (indirect) AC, technology mix of CIS, CdTe, mono crystalline and multi crystalline ; production mix, at plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | BG | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | IS | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | LT | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | DK | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | GR | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | PT | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | LV | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | LU | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | GB | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | FI | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | DE | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | PL | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | HU | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | SI | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | NO | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | AT | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | IT | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | CH | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | ES | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | NL | agg | Sphera |
Electricity from renewables unspecified AC, technology mix ; production mix, at plant ; 1kV - 60kV | SK | agg | Sphera |
Electricity from waste AC, CHP, dry flue gas treatment, without waste collection, transport and pre-treatment ; production mix, at power plant ; 1kV - 60kV | RS | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | LK | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | UA | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | CL | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | MA | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | PH | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | KR | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | HR | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | IL | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | AR | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | NI | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | TW | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | EG | agg | Sphera |
Electricity from wind power AC, technology mix of onshore and offshore ; production mix, at plant ; 1kV - 60kV | MX | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | RS | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | PK | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | TT | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | IL | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | EG | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | OM | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | MA | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | KW | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | NI | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | DZ | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | PA | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | CO | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | SA | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | VN | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | HN | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | BA | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | IQ | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | EC | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | BD | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | AE | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | KH | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | SV | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | QA | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | LK | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | KE | agg | Sphera |
Electricity grid mix AC, technology mix ; consumption mix, to consumer ; <1kV | PH | agg | Sphera |
Electricity grid mix - Central AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - Central 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix - East AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - East 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix - North AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - North 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix - Northeast AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - Northeast 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix - Northwest AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - Northwest 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix - South AC, technology mix ; consumption mix, to consumer ; <1kV | CN | agg | Sphera |
Electricity grid mix - South 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CN | agg | Sphera |
Electricity grid mix (average power plants) 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | EU-28 | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | IQ | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | BA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | RS | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | OM | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | CO | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | EC | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | PA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | ZA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | VE | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | EG | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | DZ | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | VN | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | BD | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | PY | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | MK | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | NG | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | HR | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | PK | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | HN | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | SV | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | MA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | KE | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | QA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | KW | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | TT | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | KH | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | KZ | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | IL | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | SA | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | PH | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | HK | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, to consumer ; <1kV | NI | agg | Sphera |
Electricity grid mix (direct) AC, technology mix ; consumption mix, at consumer ; <1kV | LK | agg | Sphera |
Electricity grid mix (direct) (eGRID) AC, technology mix ; consumption mix, at consumer ; <1kV | US | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | KE | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | ZA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | DZ | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | HR | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | BD | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | SA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | TT | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | MA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | CO | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | OM | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | KH | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | QA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | PK | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | HK | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | KZ | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | IQ | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | IL | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | NG | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | VE | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | VN | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | LK | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | HN | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | BA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | RS | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | MK | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | KW | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | NI | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | EG | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | PH | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | SV | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | PA | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, to consumer ; <1kV | EC | agg | Sphera |
Electricity grid mix (indirect) AC, technology mix ; consumption mix, at consumer ; <1kV | PY | agg | Sphera |
Electricity grid mix (indirect) (eGRID) AC, technology mix ; consumption mix, at consumer ; <1kV | US | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | SV | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | MK | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | PY | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | VN | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | BA | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | HR | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | KE | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | KW | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | SA | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | HK | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | RS | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | HN | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | EC | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | BD | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | DZ | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | MA | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | IL | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | KZ | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | AE | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | QA | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | IQ | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | TT | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | PA | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | CO | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | KH | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | EG | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | OM | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | NI | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | PH | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | NG | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | PK | agg | Sphera |
Electricity grid mix 1kV-60kV AC, technology mix ; consumption mix, to consumer ; 1kV - 60kV | LK | agg | Sphera |
Electrode baking petrol coke, pitch and hard coal tar ; production mix, at plant ; >99% carbon | NO | agg | Sphera |
Electrode baking petrol coke, pitch and hard coal tar ; production mix, at plant ; >99% carbon | ZA | agg | Sphera |
Electrolytic copper secondary (input heavy copper scrap 95-98% Cu) copper scrap smelting and refining ; single route, at plant ; 8.92 g/cm³, 63.55 g/mol | EU-28 | p-agg | Sphera |
Electrolytic copper secondary (input light copper scrap 90% Cu) copper scrap smelting and refining ; single route, at plant ; 8.92 g/cm³, 63.55 g/mol | EU-28 | p-agg | Sphera |
Electrolytic manganese dioxide (EMD, MnO2) using selenium from manganese ore ; production mix, at plant ; 5.03 g/cm3, 86.94 g/mol | CN | agg | Sphera |
Electrolytic manganese dioxide (EMD, MnO2) using SO2 from manganese ore ; production mix, at plant ; 5.03 g/cm3, 86.94 g/mol | CN | agg | Sphera |
Electrolytic manganese dioxide (EMD, MnO2) using SO2 mining, crushing, calcination, electrolysis, oxidation ; production mix, at plant ; 5.03 g/cm3, 86.94 g/mol | ZA | agg | Sphera |
Empty Fruit Bunches (EFB), by-products PK and CPO (price allocation, base case) technology mix ; production mix, at plant ; crude, raw kernel oil | MY | agg | Sphera |
Empty Fruit Bunches (EFB), by-products PK and CPO (price allocation, best case) technology mix ; production mix, at plant ; crude, raw kernel oil | MY | agg | Sphera |
Empty Fruit Bunches (EFB), by-products PK and CPO (price allocation, worst case) technology mix ; production mix, at plant ; crude, raw kernel oil | MY | agg | Sphera |
EPDM waste in waste incineration plant (inclu credit) waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 43,0 MJ/kg net calorific value | DE | p-agg | Sphera |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) chlorination of propene ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | DE | agg | Sphera |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | NL | agg | Sphera |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | BE | agg | Sphera |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | EU-28 | agg | Sphera |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | ES | agg | Sphera |
Epichlorohydrin Ethyleneoxide natural rubber (ECO) copolymerization of epichlorohydrin and ethylene oxide ; sigle producer, at plant ; solution rubber | DE | agg | Sphera |
Epichlorohydrin from refined glycerine refined glycerine hydrochlorination to epichlorohydrin ; single route, at plant ; 1.18 g/cm3, 92.52 g/mol | US | agg | Sphera |
Epoxidation of soybean oil (ESBO) - open input soy bean (approximation) catalytic epoxidation ; production mix, at plant ; 0.994 g/cm3 | EU-28 | p-agg | Sphera |
Epoxidized Methyl Soyate by-prod Glycerine (C mass allocated - approximation) by-product glycerine, soy oil production, refining, transesterification ; production mix, at plant ; 70,9% carbon content (67,15% bio) | EU-28 | agg | Sphera |
Epoxised soybean oil (ESBO) (approximation) epoxydising soy bean oil ; single route, at plant ; 0.994 g/cm3 | EU-28 | agg | Sphera |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin ; production mix, at plant ; approx. 1.15 g/cm3, 29.73 MJ/kg | IT | agg | Sphera |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin ; production mix, at plant ; approx. 1.15 g/cm3, 29.73 MJ/kg | NL | agg | Sphera |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin ; production mix, at plant ; approx. 1.15 g/cm3, 29.73 MJ/kg | ES | agg | Sphera |
Ethane refinery gas separation ; single route, at plant ; 1.36 g/l, 30.07 g/mol | US | agg | Sphera |
Ethanol (96%) (catalytic hydrogenation with phosphoric acid) catalytic hydrogenation with phosphoric acid ; single route, at plant ; 96 % concentrated | DE | agg | Sphera |
Ethanol (96%) (hydrogenation with nitric acid) hydrogenation with nitric acid ; single route, at plant ; 96 % concentrated | EU-28 | agg | Sphera |
Ethanol (96%) (hydrogenation with nitric acid) hydrogenation with nitric acid ; single route, at plant ; 96 % concentrated | NL | agg | Sphera |
Ethene (ethylene) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | KR | agg | Sphera |
Ethene (ethylene) steam cracker, from naphtha ; production mix, at plant ; 1.178 kg/m3, 28 g/mol | PL | agg | Sphera |
Ethene (ethylene) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | AU | agg | Sphera |
Ethene (ethylene) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | MY | agg | Sphera |
Ethene (ethylene) (approximation) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | CN | agg | Sphera |
Ethene (ethylene) (approximation) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | SA | agg | Sphera |
Ethene (ethylene) (approximation) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | BE | agg | Sphera |
Ethene (ethylene) (Oxi) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | US | agg | Sphera |
Ethyl acetate by-product polyvinyl butyral (PVB) reaction of butyric aldehyde with polyvinyl alcohol, by product polyvinyl butyral ; single route, at plant ; 0.897 g/cm³, 88.11 g/mol | DE | agg | Sphera |
Ethyl acetate by-product polyvinyl butyral (PVB) reaction of butyric aldehyde with polyvinyl alcohol, by product polyvinyl butyral ; single route, at plant ; 0.897 g/cm³, 88.11 g/mol | NL | agg | Sphera |
Ethyl benzene liquid phase alkylation ; production mix, at plant ; 0.87 g/cm3, 106.17 g/mol | ES | agg | Sphera |
Ethyl benzene liquid phase alkylation ; production mix, at plant ; 0.87 g/cm3, 106.17 g/mol | EU-28 | agg | Sphera |
Ethyl benzene liquid phase alkylation ; production mix, at plant ; 0.87 g/cm3, 106.17 g/mol | CZ | agg | Sphera |
Ethyl carbonate reaction of ethylene oxide and carbon dioxide ; production mix, at plant ; 1.32 g/cm3, 88.06 g/mol | DE | agg | Sphera |
Ethylbenzene (liquid phase alkylation) (approximation) liquid phase alkylation ; production mix, at plant ; 0.87 g/cm, 106.17 g/mol | IT | agg | Sphera |
Ethylbenzene (liquid phase alkylation) (approximation) liquid phase alkylation ; production mix, at plant ; 0.87 g/cm, 106.17 g/mol | BE | agg | Sphera |
Ethylbenzene/Styrene in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 39,1 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Ethylen Propylen Dien Elastomer (EPDM) suspension polymerisation ; production mix, at plant ; Synthetic rubber, 0.90 to >2.00 g/cm3, 36 MJ/... | US | agg | Sphera |
Ethylene (Ethene) (biobased from BR sugar cane) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | BR | agg | Sphera |
Ethylene (Ethene) (methanol to Olefin, UOP) (biobased from wood) from biobased methanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | US | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from Brazilian sugar cane) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | DE | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from corn) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | DE | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from corn) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | US | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from sugar beet) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from sugar beet) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | DE | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from US corn) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from wheat) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | US | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from wheat) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) from ethanol (biobased from wheat) dehydration of biobased ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | DE | agg | Sphera |
Ethylene (Ethene) from natural gas (methanol ton olefin, UOP) from methanol based on natural gas ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene (Ethene) via dehydration of ethanol dehydration of ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | US | agg | Sphera |
Ethylene (Ethene) via dehydration of ethanol dehydration of ethanol ; production mix, at plant ; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | Sphera |
Ethylene bis(stearamide), EBS (stoichiometric approximation) reaction of ethylene diamine with stearic acid ; production mix, at plant ; 0.99–1.01 g/cm3, 593.04 g/mol | DE | agg | Sphera |
Ethylene carbonate via carbon dioxide and ethylene oxide ; production mix, at plant ; 1.32 g/cm3, 88.06 g/mol | DE | agg | Sphera |
Ethylene carbonate (CO2 from EO) via carbon dioxide and ethylene oxide ; single route, at plant ; 1.32 g/cm3, 88.06 g/mol | JP | agg | Sphera |
Ethylene chlorohydrin (approximation) reaction of ethylene with chlorine and water ; single route, at plant ; 1.20 g/cm3, 80.51 g/mol | DE | agg | Sphera |
Ethylene dichloride (EDC) (approximation) from ethene and chlorine ; production mix, at plant ; 1.25 g/cm3, 98.95 g/mol | EU-28 | agg | Sphera |
Ethylene dichloride (EDC) (approximation) from ethene and chlorine ; production mix, at plant ; 1.25 g/cm3, 98.95 g/mol | GB | agg | Sphera |
Ethylene dichloride (EDC) (approximation) from ethene and chlorine ; production mix, at plant ; 1.25 g/cm3, 98.95 g/mol | DE | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | AU | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | DE | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | SA | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | BR | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | CN | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) (approximation) from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | MY | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) (biobased from corn) from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | EU-28 | agg | Sphera |
Ethylene glycol (from ethene and oxygen via EO) (biobased from sugar cane) oxidation of ethene with oxygen and water ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | EU-28 | agg | Sphera |
Ethylene glycol butyl ether (butoxyethanol) via ethylene oxide with butyl alcohol ; production mix, at plant ; 0.90 g/cm3, 118.18 g/mol | DE | agg | Sphera |
Ethylene glycol butyl ether (butoxyethanol) via ethylene oxide with butyl alcohol ; production mix, at plant ; 0.90 g/cm3, 118.18 g/mol | EU-28 | agg | Sphera |
Ethylene glycol butyl ether (butoxyethanol) via ethylene oxide with butyl alcohol ; production mix, at plant ; 0.90 g/cm3, 118.18 g/mol | US | agg | Sphera |
Ethylene glycol by-product ethylene oxide (EO) via O2/methane oxidation of ethylene with oxygen ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | US | agg | Sphera |
Ethylene glycol by-product Ethyleneoxide (EO) via O2/methane oxidation of ethene with oxygen and water ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | MY | agg | Sphera |
Ethylene glycol from Ethene (biobased from sugar beet) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | EU-28 | agg | Sphera |
Ethylene glycol from Ethene (biobased from sugar beet) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | DE | agg | Sphera |
Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | US | agg | Sphera |
Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | EU-28 | agg | Sphera |
Ethylene glycol from Ethene (biobased from sugar cane) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | DE | agg | Sphera |
Ethylene glycol from Ethene (biobased from US corn) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | DE | agg | Sphera |
Ethylene glycol from Ethene (biobased from US corn) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | US | agg | Sphera |
Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | EU-28 | agg | Sphera |
Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | DE | agg | Sphera |
Ethylene glycol from Ethene (biobased from wheat) and oxygen via EO from biobased ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | US | agg | Sphera |
Ethylene Methacrylic Acid Ionomer (EMAA) (high pressure autoclave) copolymerization of of ethylene and methacrylic acid ; single route, at plant ; without additives | DE | agg | Sphera |
Ethylene Methyl Acrylate (EMA) copolymerization of ethene and methacrylate ; production mix, at plant ; 0.94 g/cm3 | DE | agg | Sphera |
Ethylene Norbornen copolymer (COC, Cyclic olefine copolymers) copolymerization of ethylene and norbornene ; single producer, at plant ; density 1.02 g/cm³, solid | DE | agg | Sphera |
Ethylene oxide (EO) by-product carbon dioxide from air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | IT | agg | Sphera |
Ethylene oxide (EO) by-product carbon dioxide via air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | ES | agg | Sphera |
Ethylene propylene dien elastomer (EPDM) (biobased from BR sugar cane) copolymerisation of ethylene (biobased) and propylene ; single route, at plant ; ethylene content around 45% to 85%, 0.90 to >2.0... | EU-28 | agg | Sphera |
Ethylene Propylene Diene Elastomer (EPDM) copolymerization of ethylene and propylene ; production mix, at plant ; Synthetic rubber, 0.90 to >2.00 g/cm3, 36 MJ/... | EU-28 | agg | Sphera |
Ethylene propylene diene elastomer extrusion profile (EPDM) polymerization of ethylene and propylene, crosslinking, extrusion ; single route, at plant ; Synthetic rubber, 0.90 to >2.00 g/cm3, 36 MJ/kg... | EU-28 | agg | Sphera |
Ethylene propylene diene elastomer extrusion profile (EPDM) polymerization of ethylene and propylene, crosslinking, extrusion ; single route, at plant ; Synthetic rubber, 0.90 to >2.00 g/cm3, 36 MJ/kg... | DE | agg | Sphera |
Ethylene tetra fluor ethylene foil (ETFE) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 14,4 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Ethylene tetrafluoroethylene granulate (ETFE) copolymerization reaction of tetrafluoroethylene and ethylene ; production mix, at plant ; 100.02 g/mol per repeating unit, 1700 kg/m3 | DE | agg | Sphera |
Ethylene vinyl acetate copolymer (72% ethylene, 28% vinyl acetate) co- polymerization of ethylene and vinyl acetate ; production mix, at plant ; without additives, 72% ethylene, 28% vinyl ace... | DE | agg | Sphera |
Ethylene vinyl acetate copolymer foam co- polymerization of ethylene and vinyl acetate ; production mix, at plant ; 72% ethylene, 28% vinyl acetate | DE | agg | Sphera |
Ethylene vinyl alcohol copolymer (EVOH) hydrolysis of ethylene–vinyl acetate copolymer ; single route, at plant ; 72 g/mol per repeating unit | DE | agg | Sphera |
Ethylene vinyl alcohol copolymer (EVOH) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; EVOH waste | EU-28 | p-agg | Sphera |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia ; single route, at plant ; EDA, DETA, TETA, TEPA, PEHA | DE | agg | Sphera |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia ; single route, at plant ; EDA, DETA, TETA, TEPA, PEHA | US | agg | Sphera |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia ; single route, at plant ; EDA, DETA, TETA, TEPA, PEHA | EU-28 | agg | Sphera |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia ; single route, at plant ; EDA, DETA, TETA, TEPA, PEHA | GB | agg | Sphera |
Ethylenediaminetetraacetic acid (EDTA) (approximation) Cyanomethylation of ethylene diamine ; single route, at plant ; 0.86 g/cm3, 292.24 g/mol | DE | agg | Sphera |
Ethylene-t-Butylether (ETBE) from C4 reaction of isobutene ; single route, at plant ; 0.74 g/cm3, 102.18 g/mol | DE | agg | Sphera |
Ethylene-t-Butylether (ETBE) from C4 (biobased from wheat) reaction of biobased ethanol and isobutene ; single route, at plant ; 0.74 g/cm3, 102.18 g/mol | DE | agg | Sphera |
Ethylhexyl acrylate esterification of acrylic acid and 2-ethylhexanol from propylene ; production mix, at plant ; 0.89 g/cm3, 184.28 g/mol | EU-28 | agg | Sphera |
Ethylhexyl acrylate esterification of acrylic acid and 2-ethylhexanol from propylene ; production mix, at plant ; 0.89 g/cm3, 184.28 g/mol | DE | agg | Sphera |
Ethyne (acetylene) from calcium carbide via calcium carbide ; single route, at plant ; 1.18 g/l, 26.04 g/mol | CN | agg | Sphera |
Ethyne (acetylene) from natural gas SACHSSE-BARTHOLOME process, from natural gas ; production mix, at plant ; 1.097 kg/m3, 26.04 g/mol | CN | agg | Sphera |
Etidronic acid (HEDP) reaction of phosphorous trichloride and acetic anhydride in water ; single route, at producer ; etidronic acid without water content, molecul... | DE | agg | Sphera |
Eucalyptus plantation (30% H2O content) perennial cultivation, harvesting, air- drying ; single route, at producer ; 30% H2O content | BR | agg | Sphera |
Europium oxide primary production ; production mix, at plant ; RE95% | US | agg | Sphera |
Expanded Polystryrol/polypropylene foam packing (approximation) plasticising and mixing foam ; single route, at plant ; 70% polystyrene, 30% polypropylene | EU-28 | agg | Sphera |
Expanded Polystyrene (EPS) Foam (12 kg/m3) styrene polymerization, foaming ; production mix, at plant ; incl. flame retardant (approximation), 12 kg/m3 | US | agg | Sphera |
Expanded Polystyrene (EPS) with 1% brominated flame retardant in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 39.6 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Expanded Polystyrene (EPS) with 1% brominated flame retardant in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 39.6 MJ/kg net calorific value | DE | p-agg | Sphera |
Explosives (ANFO) production, explosion ; single route, to consumer ; blasting agent, explosive; 0.8g/cm3 | EU-28 | agg | Sphera |
Facade panel (12mm) on landfill landfill including leachate treatment and without collection, transport and pre-treatment ; production mix (region specific sites), ... ; C 68.8 kg, H 6.2 kg, O 12.3 kg... | EU-28 | p-agg | Sphera |
Facade panel (20mm) on landfill landfill including leachate treatment and without collection, transport and pre-treatment ; production mix (region specific sites), ... ; C 79.3 kg, H 7.0 kg, O 14.1 kg... | EU-28 | p-agg | Sphera |
Fan HDD (120X25mm, PWM) technology mix ; production mix, at plant ; 120X25mm, PWM | DE | agg | Sphera |
Fan PSU (78X25mm, not PWM) technology mix ; production mix, at plant ; 78X25mm, not PWM | DE | agg | Sphera |
Fatty acid from rape oil (by-product oleic acids) enzymatic hydrolysis and distillation ; single route, at plant ; 37.65 MJ/kg net calorific value | DE | agg | Sphera |
Fatty acid monosaturated from rape oil (by-product other fatty acids) enzymatic hydrolysis and distillation ; single route, at plant ; 37.65 MJ/kg net calorific value | DE | agg | Sphera |
Feather meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | ZA | agg | Sphera |
Feather meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Feather meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Feather meal from poultry (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Feldspar Open-pit mining ; Single route, at plant ; Al2O3*SiO2*Na2O | US | agg | Sphera |
Fermentation medium with sorbitol (2011) mixing components for growth medium ; production mix, at plant ; 23% sorbitol content | US | agg | Sphera |
Ferric chloride direct chlorination of iron scrap ; single route, at plant ; estimation, including chlorine recuperation | EU-28 | agg | Sphera |
Ferric chloride (approximation) direct chlorination of iron scrap ; single route, at plant ; estimation, including chlorine recuperation | DE | agg | Sphera |
Ferric oxide (FeO) via Fe2O3 via iron oxide ; production mix, at plant ; 5.75 g/cm3, 71.85 g/mol | EU-28 | agg | Sphera |
Ferric oxide mix (FeO) technology mix (via iron and via iron(3) oxide) ; production mix, at plant ; 5.75 g/cm3, 71.85 g/mol | EU-28 | agg | Sphera |
Ferrite (MnZn ferrite) shape forming and sintering ; single route, at plant ; 70% ferrite, 17% manganous oxide, 13% zinc | ES | agg | Sphera |
Ferro chrome high carbon Primary production, ore mining and beneficiation ; production mix, at plant ; 60 % chrome, high carbon ~ 6% | GLO | agg | Sphera |
Ferro chrome low carbon Primary production, ore mining and processing ; production mix, at plant ; 60 % chrome, low carbon ~ 1% | GLO | agg | Sphera |
Ferro Niobium pyrchlore ore mining and refining, carbothermic reduction and aluminothermic reduction ; single route, at plant | BR | agg | Sphera |
Ferro silicon (90% Si) primary production, smelting furnace ; production mix, at plant ; 90%, silicon | RU | agg | Sphera |
Ferro silicon (90% Si) primary production, smelting furnace ; production mix, at plant ; 90%, silicon | CN | agg | Sphera |
Ferromolybdenum mix (Mo 60%) separation, leaching, roasting ; production mix, at plant ; 60 % molybdenum content | GLO | agg | Sphera |
Ferro-phosphorus (incl. sinter) reaction of apatite with coke and silica in a low shaft electric furnace ; single producer, at plant ; 22.5% phosphorous, 7-14% vanadium pentoxide | DE | agg | Sphera |
Ferro-Vanadium Primary production, ore mining and processing ; production mix, at plant ; 80% vanadium content | ZA | agg | Sphera |
Finished leather unpainted, 1 kg - Chromium tanning (Wet Blue) - open input cattle hide Chromium tanning, after chromium tanning ; production mix, at consumer ; 1 kg, average waste water | US | p-agg | Sphera |
Fire proof stones (alumina-rich) crushing, mixing, burning ; single route, at plant ; alumina-rich | CN | agg | Sphera |
Fire proof stones (alumina-rich) crushing, mixing, burning ; single route, at plant ; alumina-rich | DE | agg | Sphera |
Fire proof stones (alumina-rich) crushing, mixing, burning ; single route, at plant ; alumina-rich | UA | agg | Sphera |
Fire proof stones (alumina-rich) crushing, mixing, burning ; single route, at plant ; alumina-rich | BR | agg | Sphera |
Fire proof stones (alumina-rich) crushing, mixing, burning ; single route, at plant ; alumina-rich | EU-28 | agg | Sphera |
Fire proof stones (alumina-rich) (approximation) crushing, mixing, burning ; single route, at plant ; alumina-rich | IN | agg | Sphera |
Fish meal fish grinding, steam cooking, mechanical oil extraction, evaporation ; single route, at plant ; 20% carbon content, 20 MJ net calorific value | US | agg | Sphera |
Flat glass Pilkington process, mixing and melting minerals ; production mix, at plant ; 2500 kg/m3 | DE | agg | Sphera |
Flax cultivation (10% H2O content) flax cultivation and harvesting ; production mix, at field border ; 10% H2O content | FR | agg | Sphera |
Flax seed cultivation (15% H2O content) flax cultivation and harvesting ; production mix, at field border ; 15% H2O content | CA | agg | Sphera |
Flexible printed wiring board, 1 layer, single sided, with FR4, chem-elec AuNi finish via the subtractive method (as opposed to additive method) ; production mix, at plant ; 1-layer flexible PWB with FR4 stiffener, chem-... | GLO | agg | Sphera |
Flexible printed wiring board,1 layer, single sided, without FR4, chem-elec AuNi finish via the subtractive method (as opposed to additive method) ; production mix, at plant ; 1-layer flexible PWB without FR4 stiffener, ch... | GLO | agg | Sphera |
Floor mopping preservative agent (ammonia-based, cleaning agents) from ammonium water and tensides ; single route, at plant ; 75% tensides, 25% ammonia water | DE | agg | Sphera |
Fluorine electrolysis of KF/HFmixtures ; single route, at plant ; 1.6965 kg/m3, 37.98 g/mol | DE | agg | Sphera |
Fluorine electrolysis of KF/HF mixtures ; single route, at plant ; gas form, 1.6965 kg/m3 at STP condistions (0°C a... | EU-28 | agg | Sphera |
Fluorine (electrolysis hydrogen fluoride) electrolysis of CaF2/HFmixtures ; single route, at plant ; gas form, 1.6965 kg/m3, 37.98 g/mol | JP | agg | Sphera |
Fluorine graphite direct fluorination of graphite ; production mix, at plant ; 31.01 g/mol | JP | agg | Sphera |
Fluorosilicic acid by-product phosphoric acid (75%) phosphoric acid wet process ; single route, at plant ; 1.46 g/cm3, 144.09 g/mol | DE | agg | Sphera |
Fluorosilicic acid by-product phosphoric acid (75%) (approximation) phosphoric acid wet process ; single route, at plant ; 1.46 g/cm3, 144.09 g/mol | US | agg | Sphera |
Fluorspar (extraction and processing) extraction and processing ; production mix, at plant ; 3.2 g/cm3 | CN | agg | Sphera |
Fluorspar (extraction and processing) extraction and processing ; production mix, at plant ; 3.2 g/cm3 | US | agg | Sphera |
Fluorspar (extraction and processing) extraction, processing, transport ; consumption mix, to consumer ; 3.2 g/cm3 | JP | agg | Sphera |
Fluorspar (extraction and processing) extraction and processing ; production mix, at plant ; 3.2 g/cm3 | MX | agg | Sphera |
Fluorspar (extraction and processing) extraction and processing ; production mix, at plant ; 3.2 g/cm3 | DE | agg | Sphera |
Fluorspar (import mix) extraction, processing, transport ; import mix, to consumer ; 3.2 g/cm3 | US | agg | Sphera |
Fluor-spar (mining and processing) extraction and processing ; production mix, at plant ; 3.2 g/cm3 | ZA | agg | Sphera |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; mineral composition | GB | agg | Sphera |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; mineral composition | CN | agg | Sphera |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; mineral composition | RO | agg | Sphera |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; mineral composition | DE | agg | Sphera |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning ; production mix, at power plant ; mineral composition | EU-28 | agg | Sphera |
Foam glass 1 cbm from mineral raw materials ; production mix, at plant ; 1 cbm | EU-28 | p-agg | Sphera |
Formaldehyde (37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | US | agg | Sphera |
Formaldehyde (HCHO; 100%) dehydrogenation of methanol ; production mix, at plant ; 100 % concentrated | FR | agg | Sphera |
Formaldehyde (HCHO; 100%) dehydrogenation of methanol ; production mix, at plant ; 100 % concentrated | NL | agg | Sphera |
Formaldehyde (HCHO; 100%) dehydrogenation of methanol ; production mix, at plant ; 100 % concentrated | IT | agg | Sphera |
Formaldehyde (HCHO; 100%) dehydrogenation of methanol ; production mix, at plant ; 100 % concentrated | GB | agg | Sphera |
Formaldehyde (HCHO; 100%) dehydrogenation of methanol ; production mix, at plant ; 100 % concentrated | MY | agg | Sphera |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | MY | agg | Sphera |
Formic acid (methane acid) 85% from methanol, carbon monoxide and water ; production mix, at plant ; 1.220 g/mL, 46.03 g/mol | EU-28 | agg | Sphera |
Gadolinium oxide primary production ; production mix, at plant ; RE95% | US | agg | Sphera |
Gallium technology mix ; production mix, at plant ; 5,9 g/cm3 | GLO | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 500 ppm sulphur | BR | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 800 ppm sulphur | CN | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | NL | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 50 ppm sulphur | MY | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | FR | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | GB | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | JP | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 150 ppm sulphur | RU | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | DE | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | AU | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | EU-28 | agg | Sphera |
Gasoline (premium) at refinery from crude oil ; production mix, at refinery ; 30 ppm sulphur | US | agg | Sphera |
Gasoline (premium) at refinery Western Australia from crude oil ; production mix, at refinery ; 50 ppm sulphur | AU | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 800 ppm sulphur | CN | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | EU-28 | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | AU | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 500 ppm sulphur | BR | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 10 ppm sulphur | JP | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 150 ppm sulphur | RU | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 150 ppm sulphur | IN | agg | Sphera |
Gasoline (regular) at refinery from crude oil ; production mix, at refinery ; 30 ppm sulphur | US | agg | Sphera |
Gasoline (regular) at refinery Western Australia from crude oil ; production mix, at refinery ; 50 ppm sulphur | AU | agg | Sphera |
Gasoline (Super) supplied and combusted [gasoline input in kg] Combustion of 1kg fuel input ; single route, at plant ; 43.2 MJ/kg net calorific value | EU-28 | agg | Sphera |
Gasoline (Super) supplied and combusted [gasoline input in kg] (direct) Combustion of 1kg fuel input ; single route, at plant ; Scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Gasoline (Super) supplied and combusted [gasoline input in kg] (indirect) Combustion of 1kg fuel input ; single route, at plant ; Scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta] Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; eta 85% | EU-28 | agg | Sphera |
Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta] (direct) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; Scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Gasoline (Super) supplied and combusted [th. energy output in MJ, 85% eta] (indirect) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; Scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Gasoline mix (premium) at refinery from crude oil and bio components ; production mix, at refinery ; 10 ppm sulphur, 6.83 wt.% bio components; 3... | NL | agg | Sphera |
Gasoline mix (premium) at refinery from crude oil and bio components ; production mix, at refinery ; 50 ppm sulphur, 0.00 wt.% bio components | MY | agg | Sphera |
Gasoline mix (premium) at refinery from crude oil and bio components ; production mix, at refinery ; 150 ppm sulphur, 0.00 wt.% bio components | RU | agg | Sphera |
Gasoline mix (premium) at refinery from crude oil and bio components ; production mix, at refinery ; 10 ppm sulphur, 12.82 wt.% bio components; ... | FR | agg | Sphera |
Gasoline mix (premium) at refinery Western Australia from crude oil and bio components ; production mix, at refinery ; 50 ppm sulphur, 1.46 wt.% bio components; 0... | AU | agg | Sphera |
Gasoline mix (regular) at refinery from crude oil and bio components ; production mix, at refinery ; 150 ppm sulphur, 0.00 wt.% bio components | RU | agg | Sphera |
Gasoline mix (regular) at refinery Western Australia from crude oil and bio components ; production mix, at refinery ; 50 ppm sulphur, 1.46 wt.% bio components; 0... | AU | agg | Sphera |
Gelatine from pork skin slaughtering and processing, pig skin via acid treatment ; single route, at plant ; about 10 % water content | EU-28 | agg | Sphera |
Generic television manufacturing (TV 65") technology mix ; production mix, at producer ; 65" Liquid Crystal Display (LCD), Panel Ass... | GLO | agg | Sphera |
Glass fibre fleece (21% UF resin) (approximation) mixing of glass fiber, UF and PMMA, fleece production ; production mix, at plant ; 21% urea formaldehyde resin | DE | agg | Sphera |
Glass fibre mesh technology mix ; production mix, at plant ; Glass fibre | CN | agg | Sphera |
Glass fibre mesh technology mix ; production mix, at plant ; Glass fibre | EU-28 | agg | Sphera |
Glass fibres from mineral components ; production mix, at plant ; Borosillicate glass / E-glass | EU-28 | agg | Sphera |
Glass fibres from mineral components ; production mix, at plant ; Borosillicate glass / E-glass | CZ | agg | Sphera |
Glass fibres from mineral components ; production mix, at plant ; Borosillicate glass / E-glass | UA | agg | Sphera |
Glass fibres from mineral components ; production mix, at plant ; Borosillicate glass / E-glass | CN | agg | Sphera |
Glass fleece from glass fibres and urea- formaldehyde- resin ; production mix, at plant ; 82% glass fibres and 18% UF resin | UA | agg | Sphera |
Glass fleece from glass fibres and urea- formaldehyde- resin ; production mix, at plant ; 82% glass fibres and 18% UF resin | CN | agg | Sphera |
Glass fleece (EN15804 A1-A3) from glass fibres and urea- formaldehyde- resin ; production mix, at plant ; 82% glass fibres and 18% UF resin | EU-28 | agg | Sphera |
Gluconobacter suboxydans (seed culture) seed medium cultivation in two steps ; single route, at plant ; two step cultivation | US | agg | Sphera |
Glucose from Straw (better case) (open elec. and th.E.) via enzymatic hydrolysis with acid pre-treatment ; single producer, at plant ; DE 20 | DE | p-agg | Sphera |
Glucose from Straw (worse case) (open elec. and th.E.) via enzymatic hydrolysis with acid pre-treatment ; single producer, at plant ; DE 20 | DE | p-agg | Sphera |
Glucose syrup from corn, 30 % H2O content Corn cultivation, grain drying, corn wet mill, glucose syrup production from corn starch slurry, dyring ; single route, at field border ; 30% H2O, syrup | US | agg | Sphera |
Glucose syrup from corn, 30 % H2O content Corn cultivation, grain drying, corn wet mill, glucose syrup production from corn starch slurry, dyring ; single route, at field border ; 30% H2O, syrup | EU-28 | agg | Sphera |
Glucose syrup from corn, 30% H2O content Corn cultivation, grain drying, corn wet mill, glucose syrup production from corn starch slurry ; single route, at field border ; 30% H2O (syrup) | CN | agg | Sphera |
Glue system mixing different adhesives ; production mix, at plant ; 33% casein glue, 33% phenol resorcin resin, 33... | DE | agg | Sphera |
Glycerin by-product Palm oil methyl ester (PME) by-product Palm oil methyl ester (PME) ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | MY | agg | Sphera |
Glycerine (87%) - KOH (13%) mixture by-product rapeseed methyl ester (RME) ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | ES | agg | Sphera |
Glycerine (from Epichlorohydrine) via epichlorohydrine ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | ES | agg | Sphera |
Glycerine (from Epichlorohydrine) via epichlorohydrine ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | NL | agg | Sphera |
Glycerine (from Epichlorohydrine) via epichlorohydrine ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | BE | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (economic allocation) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | NL | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation) by-product rapeseed methyl ester (RME) ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol, 16.2 MJ/kg net calorifi... | NL | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation) by-product rapeseed methyl ester (RME) ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (economic and C mass allocation) by-product rapeseed methyl ester (RME) ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | EU-28 | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (mass allocation) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine by-product soy methylester (SME) (economic and C mass allocation) by-product SME, soy oil production, refining, transesterification ; production mix, at plant ; 39% carbon content | EU-28 | agg | Sphera |
Glycerol ester from balm colophony esterification of glycerine with retinoic acid ; single route, at plant ; 376 g/mol | EU-28 | agg | Sphera |
Glycerol ester from balm colophony esterification of glycerine with retinoic acid ; single route, at plant ; 376 g/mol | DE | agg | Sphera |
Glycidylmethacrylate esterification of methacrylic acid with epichlorohydrin ; single route, at plant ; 1.04 g/cm3, 142.15 g/mol | DE | agg | Sphera |
Glycidylmethacrylate esterification of methacrylic acid with epichlorohydrin ; single route, at plant ; 1.04 g/cm3, 142.15 g/mol | EU-28 | agg | Sphera |
Glycidylmethacrylate - open inputs epichlorohydrin and methacrylic acid esterification of methacrylic acid with epichlorohydrin ; single route, at plant ; 1.04 g/cm3, 142.15 g/mol | DE | p-agg | Sphera |
Glycidylmethacrylate (approximation) esterification of methacrylic acid with epichlorohydrin ; single route, at plant ; 1.04 g/cm3, 142.15 g/mol | US | agg | Sphera |
Glycine (amination of chloroacetic acid) Amination of Chloroacetic acid ; single route, at plant ; molar mass: 75 g/mol, density: 1.1607 g/cm, sum ... | EU-28 | agg | Sphera |
Glycolic acid reaction of chloroacetic acid with sodium hydroxide ; production mix, at plant ; 1.49 g/cm3, 76.05 g/mol | DE | agg | Sphera |
Glyoxal 40% (Acetaldehyd route) acetaldehyde route ; single route, at plant ; 40% concentrated | DE | agg | Sphera |
Goose down, at slaughterhouse gate (economic allocation) Raw goose downs, at slaughterhouse ; production mix, at producer ; Neither washed nor processed | GLO | agg | Sphera |
Goose down, cleaned, ready for use Cleaned goose downs, ready to use ; production mix, at producer ; Not sorted into quality categories | CN | agg | Sphera |
Grain leather (unvarnished, 1 sqm/0.88 kg, PEFCR allocation) - open inputs cattle hide and energy soaking & ember, splitting, pickling, tanning, neutralization, stretching ; production mix, at plant ; 1 sqm/0.88 kg | DE | p-agg | Sphera |
Granulated Blast Furnace (BF) Slag (economic allocation) iron production, blast furnace route, by- product slag ; single route, at plant ; 2800- 4000 kg/m³ | DE | agg | Sphera |
Grey cast iron (GGG70) part (chill-mold) reduction in blast furnace, chill- mold ; single route, at plant ; GGG70 | DE | p-agg | Sphera |
Ground Granulated Blast Furnace Slag (GGBFS) (economic allocation) iron production, blast furnace route, by- product slag, grinded ; single route, at plant ; 2800- 4000 kg/m³ | DE | agg | Sphera |
Gypsum (CaSO4) highly pure by-product hydrogen fluoride highly- pure, reaction of fluorspar and sulfuric acid in rotary furnace ; single route, at plant ; 2.96 g/cm3, 136.14 g/mol | DE | agg | Sphera |
Gypsum (CaSO4) highly pure by-product hydrogen fluoride (EN15804 A1-A3) highly- pure, reaction of fluorspar and sulfuric acid in rotary furnace ; single route, at plant ; 2.96 g/cm3, 136.14 g/mol | EU-28 | agg | Sphera |
Gypsum highly pure by-product hydrogen fluoride highly- pure, reaction of fluorspar and sulfuric acid in rotary furnace ; single route, at plant ; 2.96 g/cm3, 136.14 g/mol | US | agg | Sphera |
Gypsum plaster (CaSO4-Beta-hemihydrate) (from 100% gypsum stone) gypsum stone extraction, grinding and calcination ; single route, at plant ; 145.15 g/mol | DE | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; production mix, at plant ; 172 g/mol | IN | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | MX | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; production mix, at plant ; 172 g/mol | FR | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | SA | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | JP | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | CA | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining ; production mix, at plant ; grinded and purified product | BR | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; production mix, at plant ; 172 g/mol | TH | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | ES | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | TR | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining ; production mix, at plant ; grinded and purified product | UA | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; single route, at plant ; 172 g/mol | US | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; production mix, at plant ; 172 g/mol | GB | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining ; production mix, at plant ; grinded and purified product | CN | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) open pit mining ; production mix, at plant ; 172 g/mol | IT | agg | Sphera |
Gypsum stone (CaSO4-Dihydrate) (EN15804 A1-A3)) underground and open pit mining ; production mix, at plant ; grinded and purified product | EU-28 | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.1 MJ/kg net calorific value | MY | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.5 MJ/kg net calorific value | MX | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.5 MJ/kg net calorific value | DK | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 25.6 MJ/kg net calorific value | IL | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.2 MJ/kg net calorific value | CO | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 27.5 MJ/kg net calorific value | BG | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 25.2 MJ/kg net calorific value | PH | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.0 MJ/kg net calorific value | KR | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.1 MJ/kg net calorific value | MA | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 27.0 MJ/kg net calorific value | AR | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 25.4 MJ/kg net calorific value | BA | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 27.0 MJ/kg net calorific value | HR | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 23.7 MJ/kg net calorific value | ID | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 26.0 MJ/kg net calorific value | CL | agg | Sphera |
Hard coal mix technology mix ; consumption mix, to consumer ; 23.7 MJ/kg net calorific value | CZ | agg | Sphera |
Hard coal supplied and combusted in power plant technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 26.6 MJ/kg net calorific value | EU-28 | agg | Sphera |
Hard coal supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 26.6 MJ/kg net calorific value | EU-28 | agg | Sphera |
Hard coal supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 26.6 MJ/kg net calorific value | EU-28 | agg | Sphera |
Hard disk drive (HDD), 2.5", 1 platter, 2 sides, 7 mm high technology mix ; production mix, at producer ; 2.5", 1 platter, 2 sides, 7 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 2.5", 2 platters, 4 sides, 9.5 mm high technology mix ; production mix, at producer ; 2.5", 2 platters, 4 sides, 9.5 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 2.5", 3 platters, 6 sides, 12.5 mm high technology mix ; production mix, at producer ; 2.5", 3 platters, 6 sides, 12.5 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 2.5", 4 platters, 8 sides, 15 mm high technology mix ; production mix, at producer ; 2.5", 4 platters, 8 sides, 15 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 1 platter, 1 side, 26 mm high technology mix ; production mix, at producer ; 3.5", 1 platter, 1 side, 26 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 1 platter, 2 sides, 26 mm high technology mix ; production mix, at producer ; 3.5", 1 platter, 2 sides, 26 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 2 platters, 4 sides, 26 mm high technology mix ; production mix, at producer ; 3.5", 2 platters, 4 sides, 26 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 3 platters, 6 sides, 26 mm high technology mix ; production mix, at producer ; 3.5", 3 platters, 6 sides, 26 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 4 platters, 8 sides, 26 mm high technology mix ; production mix, at producer ; 3.5", 4 platters, 8 sides, 26 mm high | GLO | agg | Sphera |
Hard disk drive (HDD), 3.5", 5 platters, 10 sides, 26 mm high technology mix ; production mix, at producer ; 3.5", 5 platters, 10 sides, 26 mm high | GLO | agg | Sphera |
Hazardous waste (non-specific) (C rich, worst case scenario incl. landfill) incineration, macroencapsulation, vitrification, transport and landfill ; single route, at plant ; rich in C | GLO | agg | Sphera |
Hazardous waste (non-specific) (no C, worst case scenario incl. landfill) incineration, macroencapsulation, vitrification, transport and landfill ; single route, at plant ; no C | GLO | agg | Sphera |
Heavy Fuel Oil (HFO) supplied and combusted in power plant technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 40.44 MJ/kg net calorific value | EU-28 | agg | Sphera |
Heavy Fuel Oil (HFO) supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 40.44 MJ/kg net calorific value | EU-28 | agg | Sphera |
Heavy Fuel Oil (HFO) supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 40.44 MJ/kg net calorific value | EU-28 | agg | Sphera |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil ; production mix, at refinery ; 1 wt.% sulphur | NL | agg | Sphera |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil ; production mix, at refinery ; 1 wt.% sulphur | MY | agg | Sphera |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil ; production mix, at refinery ; 1 wt.% sulphur | RU | agg | Sphera |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil ; production mix, at refinery ; 2.5 wt.% sulphur | RU | agg | Sphera |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil ; production mix, at refinery ; 2.5 wt.% sulphur | NL | agg | Sphera |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil ; production mix, at refinery ; 2.5 wt.% sulphur | MY | agg | Sphera |
Heavy vacuum residues (HVR) at refinery from crude oil ; production mix, at refinery ; 35 MJ/kg net calorific value | EU-28 | agg | Sphera |
Helium (gaseous) cryogenic extraction from natural gas ; single route, at plant ; 0,1785 kg/m3, 4 g/mol | DE | agg | Sphera |
Helium (liquid) Collins cycle (compression, precooling and expansion in different stages) ; single producer, at plant ; boiling point of He -269°C | DE | agg | Sphera |
Hemp complete plant cultivation (15% H2O content) sowing, fertilizing, soil cultivation, harvesting ; single route, at field border ; 15% H2O | DE | agg | Sphera |
Hemp seed cultivation with catch crop (15% H2O content) sowing, fertilizing, soil cultivation, harvesting ; single route, at field border ; 15% H2O | DE | agg | Sphera |
Hemp seed with catch crop hemp cultivation with catch crop ; production mix, at field border ; 15% H2O content | DE | agg | Sphera |
Hemp straw cultivation (10% H2O content) hemp cultivation ; production mix, at field border ; 10% H2O content | DE | agg | Sphera |
Hemp straw with catch crop hemp cultivation with catch crop ; production mix, at field border ; 12% H2O content | DE | agg | Sphera |
Hemp with catch crop hemp cultivation with catch crop ; production mix, at field border ; 15% H2O content | DE | agg | Sphera |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine ; single route, at plant ; 643.71 g/mol | CN | agg | Sphera |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine ; single route, at plant ; 643.71 g/mol | US | agg | Sphera |
Hexafluoroisopropanol (HFIP) (approximation) Acetone route (Chlorination, Fluorination and Hydrogenation) ; single route, at producer ; 168.038 g/mol | JP | agg | Sphera |
Hexamethylene diamine (HMDA; from butadiene via adiponitrile) HMDA via hydrogenation of adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | BE | agg | Sphera |
Hexamethylene diisocyanate (HMDI) by-product HCl from hexamethylenediamine (HDI) by phosgenation ; single route, at plant ; 1.047 g/cm3, 168 g/mol | DE | agg | Sphera |
Hexamethylene diisocyanate (HMDI) by-product HCl from hexamethylenediamine (HDI) by phosgenation ; single route, at plant ; 1.047 g/cm3, 168 g/mol | EU-28 | agg | Sphera |
Hexamethylene imine by-product HMDA via butadiene by-product in HMDA production, HMDA route: from butadiene via adiponitrile ; single route, at plant ; 0.88 g/cm3, 99.17 g/mol | DE | agg | Sphera |
Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile) HMDA via hydrogenation of adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | US | agg | Sphera |
Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile) HMDA via hydrogenation of adiponitrile ; single route, at plant ; 0.84 g/cm3, 116.20 g/mol | CN | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene ; single route, at plant ; 0.84 g/cm3, 116.20 g/mol | US | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene ; single route, at plant ; 0.84 g/cm3, 116.20 g/mol | FR | agg | Sphera |
Hexamethylenimine by-product HMDA from butadiene via dichlorobutene from butadiene ; single route, at plant ; 0.88 g/cm3, 99.17 g/mol | FR | agg | Sphera |
Hexane in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; 44.5 MJ/kg net calorific value | EU-28 | p-agg | Sphera |
Hexanediol diglycidyl ether (approximation) coupling process ; single route, at plant ; 230.3 g/mol | DE | agg | Sphera |
Hexanediol diglycidyl ether (approximation) coupling process ; single route, at plant ; 230.3 g/mol | EU-28 | agg | Sphera |
Hexanoic acid production from refined coconut oil (approximation) Produced from hydrolysed coconut oil ; single route, at consumer ; 116.6 g/mol, 62% carbon content | EU-28 | agg | Sphera |
Hexanoic acid production from refined palm kernel oil (approximation) Produced from hydrolysed palm oil ; single route, at consumer ; 116.6 g/mol, 62% carbon content | EU-28 | agg | Sphera |
High alumina cement (HAC) from bauxite and limestone via furnace process ; production mix, at plant ; 35- 40% lime, 40- 50% alumina, <15% iron oxi... | US | agg | Sphera |
High performance film (Polyether ether ketone) Plastic extruding, melting, casting and mechanical forming ; single route, at plant ; 1.32 g/cm3, 290.31 g/mol per repeating unit | DE | agg | Sphera |
High performance film (Polyetherimide) Plastic extruding, melting, casting and mechanical forming ; single route, at plant ; 1.27 g/cm3, 592 g/mol per repeating unit | DE | agg | Sphera |
High performance film (Polyphenylene sulfide) Plastic extruding, melting, casting and mechanical forming ; single route, at plant ; 1.35 g/cm3,110 g/mol per repeating unit | DE | agg | Sphera |
High performance film (polypropylene/polyethylene membrane/foil) Plastic extruding, melting, casting and mechanical forming ; single route, at plant ; 1.08 g/cm3 | DE | agg | Sphera |
High performance film (polyvinyl butyral) Plastic extruding, melting, casting and mechanical forming ; single route, at plant ; 1.08 g/cm3, 28 MJ/kg net calorific value | DE | agg | Sphera |
High performance film (PVB, LCP, Polyacrylate, PEEK, PEI, Polyethersulfide) - open input granulate Plastic extruding, melting, casting and mechanical forming ; single producer, at plant ; 28 MJ/kg net calorific value | DE | p-agg | Sphera |
High purity alumina (HPA) dissolving of aluminium metal ; production mix, at plant ; 3.94 g/cm3, 101.96 g/mol | DE | agg | Sphera |
Hollow Polymer Spheres Expanded polymerisation, blowing ; single route, at producer ; spherically formed particles with a thermopla... | EU-28 | agg | Sphera |
Hominy (nixtamal, approximation) intensive cultivation, conventional nixtamization process ; production mix, at plant ; 12% moisture content | US | agg | Sphera |
Hydrazine hydrate/hydrazine Bayer Ketazine Process ; production mix, at plant ; 1.02 g/cm3, 32.05 g/mol | DE | agg | Sphera |
Hydrobromic acid by-product tetrabromo bisphenol A Hydrobromic acid by-product tetrabromo bisphenol A ; production mix, at plant ; 48% | DE | agg | Sphera |
Hydrobromic acid by-product tetrabromo bisphenol A Hydrobromic acid by-product tetrabromo bisphenol A ; production mix, at plant ; 48% | EU-28 | agg | Sphera |
Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl) reaction of chlorine and propene ; single route, at plant ; 100% HCl | EU-28 | agg | Sphera |
Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl) reaction of chlorine and propene ; single route, at plant ; 100% HCl | DE | agg | Sphera |
Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl) reaction of chlorine and propene ; single route, at plant ; 100% HCl | MY | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride ; single route, at plant ; 100% HCl | DE | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride ; single route, at plant ; 100% HCl | MY | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride ; single route, at plant ; 100% HCl | EU-28 | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane ; single route, at plant ; 100% HCl | MY | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane ; single route, at plant ; 100% HCl | DE | agg | Sphera |
Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane ; single route, at plant ; 100% HCl | EU-28 | agg | Sphera |
Hydrochloric acid (20%) by-product chlorobenzene from chlorobenzene ; single route, at plant ; 20% concentration | MY | agg | Sphera |
Hydrochloric acid (20%) by-product chlorobenzene from chlorobenzene ; single route, at plant ; 20% concentration | DE | agg | Sphera |
Hydrochloric acid (20%) by-product chlorobenzene from chlorobenzene ; single route, at plant ; 20% concentration | EU-28 | agg | Sphera |
Hydrochloric acid (20%), by-product dichloromethane chlorination of methyl chloride ; production mix, at plant ; 20% concentrated | DE | agg | Sphera |
Hydrochloric acid (32%), by-product Methylene diphenyl diisocyanate (MDI), methanol phosgenation of methylenedianiline ; single route, at plant ; 32% concentrated | DE | agg | Sphera |
Hydrochloric acid (32%), by-product Methylene diphenyl diisocyanate (MDI), methanol phosgenation of methylenedianiline ; single route, at plant ; 32% concentrated | BE | agg | Sphera |
Hydrochloric acid (32%), by-product Methylene diphenyl diisocyanate (MDI), methanol phosgenation of methylenedianiline ; single route, at plant ; 32% concentrated | EU-28 | agg | Sphera |
Hydrochloric acid (phosgenation) by-product toluene diamine (TDA),Toluene diisocyanate phosgenation of toluene diamine ; single producer, at plant ; 32 % concentrated | GB | agg | Sphera |
Hydrochloric acid (phosgenation) by-product toluene diamine (TDA),Toluene diisocyanate phosgenation of toluenediamine, from carbon monoxide, chlorine, hydrogen and dinitrotoluene ; single route, at plant ; 32% concentrated | IT | agg | Sphera |
Hydrochloric acid 100% (primarily from chlorine) combustion of hydrogen with chlorine ; production mix, at plant ; 100% HCl | DE | agg | Sphera |
Hydrochloric acid 100% (primarily from chlorine) combustion of hydrogen with chlorine ; production mix, at plant ; 100% HCl | BR | agg | Sphera |
Hydrochloric acid 100% (primarily from chlorine) combustion of hydrogen with chlorine ; production mix, at plant ; 100% HCl | CN | agg | Sphera |
Hydrochloric acid 100% (primarily from chlorine) (approximation) combustion of hydrogen with chlorine ; production mix, at plant ; 100% HCl | IN | agg | Sphera |
Hydrochloric acid 32% (primarily from chlorine, H2 Cracker) combustion of hydrogen with chlorine, dissolution in water ; production mix, at plant ; 32% | US | agg | Sphera |
Hydrochloric acid 32% (primarily from chlorine, H2 Steam Reforming) primarily from chlorine ; production mix, at plant ; 32 % concentrated | JP | agg | Sphera |
Hydrochloric acid 37% (primarily from chlorine, H2 Cracker) combustion of hydrogen with chlorine, dissolution in water ; production mix, at plant ; 37% concentrated | DE | agg | Sphera |
Hydrochloric acid aq. 32% by-product Methylene diphenyl diisocyanate (MDI), Methanol phosgenation of methylenedianiline ; single route, at plant ; 32% concentrated | US | agg | Sphera |
Hydrochloric acid by-product chlorobenzene from chlorobenzene ; single route, at plant ; 20% concentration | BR | agg | Sphera |
Hydrochloric acid by-product methylene diphenyl diisocyanate (MDI), methanol phosgenation of methylenedianiline ; single route, at plant ; 32% concentrated | FR | agg | Sphera |
Hydrochloric acid mix (100%) technology mix ; consumption mix, to consumer ; 100% HCl | EU-28 | agg | Sphera |
Hydrochloric acid mix (37%) technology mix ; production mix, at plant ; 32% concentrated | DE | agg | Sphera |
Hydrogen (50% steam reforming, 50% electrolysis, highly pure, liquid) technology mix (electrolysis and steam reforming of methanol) ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen (95% steam reforming, 5% steam cracker) technology mix ; production mix, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific... | US | agg | Sphera |
Hydrogen (chlorine-alkali-electrolysis, membrane, mass allocated) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | EU-28 | agg | Sphera |
Hydrogen (cracker) steam cracking ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | NL | agg | Sphera |
Hydrogen (cracker) (mass allocation) steam cracking ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | DE | agg | Sphera |
Hydrogen (electrolysis, highly pure, liquid) electrolytical cleavage of water ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen (steam cracker) steam cracking ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | FR | agg | Sphera |
Hydrogen (steam cracker) steam cracking ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3, 120 MJ/kg net calorific v... | JP | agg | Sphera |
Hydrogen (steam reforming methanol, highly pure) steam reforming of methanol ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen (steam reforming natural gas and methanol, highly pure) steam reforming of natural gas and methanol ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | IN | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | PT | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | AU | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | CN | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | NO | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | SE | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | JP | agg | Sphera |
Hydrogen (steam reforming natural gas) Steam reforming - natural gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | CZ | agg | Sphera |
Hydrogen (steam reforming natural gas) steam reforming, from natural gas ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | BR | agg | Sphera |
Hydrogen (steam reforming natural gas) steam reforming, from natural gas ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | ES | agg | Sphera |
Hydrogen (Steamreforming natural gas) steam reforming, from natural gas ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | BE | agg | Sphera |
Hydrogen (synthesis gas (H2:CO 1:1) over wood gasification) water gas shift reaction, synthesis gas produced by wood gasificiation ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | EU-28 | agg | Sphera |
Hydrogen (synthesis gas (H2:CO 2:1) over coal gasification) water gas shift reaction, synthesis gas produced by coal gasificiation ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | EU-28 | agg | Sphera |
Hydrogen (via synthesis gas) from synthesis gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | FR | agg | Sphera |
Hydrogen (via synthesis gas) from synthesis gas ; production mix, at plant ; 0.0899 kg/m3, 2 g/cm3 | DE | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | RU | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | MY | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | DE | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | IN | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | NL | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | BR | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | JP | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | CN | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | AU | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg | GB | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | FR | agg | Sphera |
Hydrogen at refinery from crude oil ; production mix, at refinery ; 120 MJ/kg net calorific value | EU-28 | agg | Sphera |
Hydrogen cyanide (prussic acid) technology mix ; production mix, at plant ; 0.687 g/mL, 27 g/mol | EU-28 | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | BE | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | NL | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | GB | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | EU-28 | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | US | agg | Sphera |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process ; production mix, at plant ; 0.687 g/cm3, 27.03 g/mol | FR | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | GB | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | DE | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | US | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | FR | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | NL | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | EU-28 | agg | Sphera |
Hydrogen cyanide (prussic acid, BMA process) BMA process ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | BE | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | DE | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | GB | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | EU-28 | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | FR | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | BE | agg | Sphera |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate (price allocated) ammoxidation of propene ; single route, at plant ; 0.687 g/cm3, 27.03 g/mol | US | agg | Sphera |
Hydrogen fluoride by-product gypsum highly pure conversion of dried fluorspar with sulphuric acid ; production mix, at plant ; 20.01 g/mol | US | agg | Sphera |
Hydrogen fluoride by-product gypsum highly pure conversion of dried fluorspar with sulphuric acid ; production mix, at plant ; 20.01 g/mol | EU-28 | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, 11% H2 allocated) chlorine alkali electrolysis, membrane ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | DE | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, 11% H2 allocated, 36% Cl2, 53% NaOH) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, 11% H2 allocated, 36% Cl2, 53% NaOH) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | EU-28 | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, 11% H2 allocated, 36% Cl2, 53% NaOH) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | DE | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, mass allocated) chlorine alkali electrolysis, membrane ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | DE | agg | Sphera |
Hydrogen from chlorine-alkali-electrolysis (membrane, mass allocated) from chlorine-alkali electrolysis (membrane) ; single route, at plant ; 0.0899 kg/m3, 2 g/cm3 | US | agg | Sphera |
Hydrogen from synthesis gas over coal gasification steam reforming, hard coal ; single route, at plant ; 0.0899 kg/m3, 2 g/mol, 120 MJ/kg net calorific v... | CN | agg | Sphera |
Hydrogen peroxide (100%; H2O2) (Hydrogen from steam reforming) anthraquinone process ; production mix, at plant ; 100% concentrated | DE | agg | Sphera |
Hydrogen peroxide (40% H2O2) anthraquinone process ; production mix, at plant ; 40% concentrated | BE | agg | Sphera |
Hydrogen peroxide aq. (highly pure, 30%) H2O2 purification by ion exchange resin ; single route, at plant ; 1.11 g/cm3, 34.02 g/mol | US | agg | Sphera |
Hydrogen peroxide mix Anthraquinone process ; production mix, at plant ; 1.11 g/cm3, 34.02 g/mol | EU-28 | agg | Sphera |
Hydrogen sulphide reaction of hydrogen and sulphur ; single route, at plant ; 1.36 g/l, 34.08 g/mol | EU-28 | agg | Sphera |
Hydrogen Sulphide reaction of hydrogen and sulphur ; single route, at plant ; 1.36 g/l, 34.08 g/mol | JP | agg | Sphera |
Hydrogen Sulphide reaction of hydrogen and sulphur ; single route, at plant ; 1.36 g/l, 34.08 g/mol | DE | agg | Sphera |
Hydrogen Sulphide reaction of hydrogen and sulphur ; single route, at plant ; 1.36 g/l, 34.08 g/mol | US | agg | Sphera |
Hydrolysis resistant coating (approximation) - open input synthetic leather hydrolysis resistant coating ; single route, at plant ; coating layer in finished synthetic leather prod... | US | p-agg | Sphera |
Hydrolysis resistant coating (approximation) - open input synthetic leather hardened hydrolysis resistant coating ; single route, at plant ; coating layer in finished synthetic leather prod... | EU-28 | p-agg | Sphera |
Hydroquinone (oxidation P-DIPB) P-DIPB oxidation, diisopropyl bis hydroperoxide cleavage ; single route, at plant ; 1.3 g/cm3, 110.11 g/mol | EU-28 | agg | Sphera |
Hydrotreated Oil from beef tallow remdering, tallow processing, transport, pretreatment, hydroprocessing ; single route, at plant ; 780 kg/m3, 44 MJ/kg net calorific value | FI | agg | Sphera |
Hydrotreated Oil from beef tallow (tallow production burden free) tallow processing, transport, pretreatment, hydroprocessing ; single route, at plant ; 780 kg/m3, 44 MJ/kg net calorific value | FI | agg | Sphera |
Hydrotreated Vegetable oil (HVO) from palm oil palm oil processing, transport, pretreatment, hydroprocessing ; single route, at plant ; 780 kg/m3, 44 MJ/kg net calorific value | FI | agg | Sphera |
Hydrotreated Vegetable oil (HVO) from rapeseed oil rapeseed oil processing, transport, pretreatment, hydroprocessing ; single route, at plant ; 780 kg/m3, 44 MJ/kg net calorific value | FI | agg | Sphera |
Hydroxybenzoic acid alkali phenoxide route ; single producer, at plant ; density 1.46 g/cm³, 138.121 g/mol | EU-28 | agg | Sphera |
Hydroxybenzoic acid alkali phenoxide route ; single producer, at plant ; density 1.46 g/cm³, 138.121 g/mol | DE | agg | Sphera |
Hydroxybenzoic acid alkali phenoxide route ; single producer, at plant ; density 1.46 g/cm³, 138.121 g/mol | US | agg | Sphera |
Hydroxyethylenemethacrylate reaction of methacrylic acid and ethylene oxide ; single route, at plant ; 1.07 g/cm3, 130.14 g/mol | DE | agg | Sphera |
Hydroxyethylenemethacrylate reaction of methacrylic acid and ethylene oxide ; single route, at plant ; 1.07 g/cm3, 130.14 g/mol | EU-28 | agg | Sphera |
Hydroxyl ammonium sulphate from nitrogen oxides, hydrogen and sulphuric acid ; single route, at plant ; 1.88 g/cm3, 164.14 g/mol | DE | agg | Sphera |
Hydroxypentamethylpiperidin (HPMP) 65% catalytic hydration of tetramethyoxopiperidin, methylation of hydroxytetramethylpiperidin ; single route, at plant ; 65% concentrated | CH | agg | Sphera |
Hydroxypivaldehyde (approximation) aldol addition of butyraldehyde and formaldehyde ; single route, at plant ; 102.13 g/mol | DE | agg | Sphera |
Hydroxytetramethylpiperidin (HTMP) 65% hydrogenation of triacetonamine ; single route, at plant ; 65% concentrated | CH | agg | Sphera |
Incineration of Municipal waste (Credited) waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; Municipal waste incineration | EU-28 | agg | Sphera |
Incineration of Municipal waste (Credited) waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment ; production mix (region specific plants),... ; Municipal waste incineration | DE | agg | Sphera |
Indanthrone blue (Blue 4) self-condensation of 2-aminoanthraquinone ; single route, at producer ; 1.6 g/ml, 442.43 g/mol | US | agg | Sphera |
Industrial wood mix (25 % moisture content, 20% H2O content) Forest cultivation, plantation maintanance ; production mix, at producer (different t... ; Mix of spruce-, beech-, -oak a... | EU-28 | agg | Sphera |
Industrial wood Pine (long) (0 % moisture content, 0 % H2O content) Forest cultivation, plantation maintanance ; production mix, at producer ; dry matter - 0 % moisture content / 0 % H2O... | DE | agg | Sphera |
Industrial wood Spruce (long) (0 % moisture content / 0 % H2O content) Forest cultivation, plantation maintanance ; production mix, at producer ; dry matter- 0 % moisture content / 0 % H2O ... | DE | agg | Sphera |
Iodine pentafluoride direct fluorination of molten iodine ; single route, at producer ; 221.89 g/mol, 3.25 g/cm3 | EU-28 | agg | Sphera |
Iodine pentafluoride direct fluorination of molten iodine ; single route, at producer ; 221.89 g/mol, 3.25 g/cm3 | DE | agg | Sphera |
Iodine pentafluoride (approximation) direct fluorination of molten iodine ; single route, at producer ; 221.89 g/mol, 3.25 g/cm3 | US | agg | Sphera |
Ion exchange resin (approximation) sulfonation of polystyrene ; single route, at plant ; 0.801 g/cm3 | DE | agg | Sphera |
Ion exchange resin (approximation) sulfonation of polystyrene ; single route, at plant ; 0.801 g/cm3 | US | agg | Sphera |
Ionomeres copolymerization of of ethylene and methacrylic acid ; single route, at plant ; 0.95 g/cm3 | DE | agg | Sphera |
Iron (II) sulphate reacting iron ore with dilute sulphuric acid ; single route, at plant ; 2.84 g/cm3, 151.91 g/mol | DE | agg | Sphera |
Iron (III) chloride (ferric chloride) chlorination of scrap iron ; production mix, at plant ; 2.898 g/cm3 (anhydrous) | US | agg | Sphera |
Iron (III) chloride (ferric chloride) chlorination of scrap iron ; production mix, at plant ; 2.898 g/cm3 (anhydrous) | CN | agg | Sphera |
Iron ore-mix iron ore mining and processing ; import mix, to consumer ; 5.00 g/cm3, 231.53 g/mol | CN | agg | Sphera |
Iron ore-mix iron ore mining and processing ; import mix, to consumer ; 5.00 g/cm3, 231.53 g/mol | JP | agg | Sphera |
Iron ore-mix iron ore mining and processing ; import mix, to consumer ; 5.00 g/cm3, 231.53 g/mol | DE | agg | Sphera |
Iron oxide (Fe2O3) dissolving iron ore in acid ; single route, at plant ; 5.24 g/cm3, 159.70 g/mol | CN | agg | Sphera |
Iron oxide (Fe2O3) from iron ore dissolving iron ore in acid ; single route, at plant ; 5.24 g/cm3, 159.70 g/mol | DE | agg | Sphera |
Iron oxide (ferrite) (Fe2O3) electrolytical ; single route, at plant ; 5.24 g/cm3, 159.70 g/mol | DE | agg | Sphera |
Isobutene by-product methylene-t-butylether (MTBE) of C4 raffinate with n-butene Isomerisation acid-catalyzed addition of methanol ; production mix, at plant ; 0.58 g/cm3, 56.12 g/mol | CN | agg | Sphera |
Isobutene by-product methylene-t-butylether (MTBE) of C4 raffinate with n-butene Isomerisation acid-catalyzed addition of methanol ; production mix, at plant ; 0.58 g/cm3, 56.12 g/mol | DE | agg | Sphera |
Isobutylene (Butyl rubber) by dispersion polymerization dispersion polymerization ; single route, at plant ; 56.11 g/mol, 0.59 g/cm3 | DE | agg | Sphera |
Isobutylene (Butyl rubber) by dispersion polymerization dispersion polymerization of isoprene and isobutene ; production mix, at plant ; 95- 99 mol-% isobutene and 1–5 mol-% isoprene | US | agg | Sphera |
Isobutyraldehyde by-product butanol Oxo process, by-product butanol from propylene with rhodium catalyst ; production mix, at plant ; 0.80 g/cm3, 72.11 g/mol, 31.6 MJ/kg | DE | agg | Sphera |
Isobutyraldehyde by-product butanol Oxo process, by-product butanol from propylene with rhodium catalyst ; production mix, at plant ; 0.80 g/cm3, 72.11 g/mol, 31.6 MJ/kg net calori... | US | agg | Sphera |
Isobutyraldehyde by-product butanol Oxo process, by-product butanol from propylene with rhodium catalyst ; production mix, at plant ; 0.80 g/cm3, 72.11 g/mol, 31.6 MJ/kg net calori... | CN | agg | Sphera |
Isobutyraldehyde by-product butanol Oxo process, by-product butanol from propylene with rhodium catalyst ; production mix, at plant ; 0.80 g/cm3, 72.11 g/mol, 31.6 MJ/kg net calori... | EU-28 | agg | Sphera |
Isooctene (di-n-butene) via n-butene dimerization_Octol process Octol Process, from n- butene ; single route, at plant ; 112.22 g/mol | DE | agg | Sphera |
Isooctene via C4 oligomerization (polygas) C4 oligomerisation ; single route, at plant ; 112.22 g/mol | DE | agg | Sphera |
Isophorone diisocyanate (IPDI) from acetone ; single route, at plant ; 1.06 g/cm3, 222.3 g/mol | EU-28 | agg | Sphera |
Isophorone diisocyanate (IPDI) from acetone ; single route, at plant ; 1.06 g/cm3, 222.3 g/mol | DE | agg | Sphera |
Isophoronediamine (IPDA) Isophorone nitrile route ; single route, at plant ; 0.92 g/cm3, 170.30 g/mol | EU-28 | agg | Sphera |
Isophoronediamine (IPDA) Isophorone nitrile route ; single route, at plant ; 0.92 g/cm3, 170.30 g/mol | DE | agg | Sphera |
Isophthalic acid Amoco process, oxidation of p- xylene ; single producer, at plant ; 1.53 g/cm3, 166.14 g/mol | DE | agg | Sphera |
Isophthalic acid Amoco process, oxidation of p- xylene ; single producer, at plant ; 1.53 g/cm3, 166.14 g/mol | US | agg | Sphera |
Isophthalic acid Amoco process, oxidation of p- xylene ; single producer, at plant ; 1.53 g/cm3, 166.14 g/mol | EU-28 | agg | Sphera |
Isoprene (from C5 stream separation) from C5 stream separation ; single route, at plant ; 0.68 g/cm3, 68.12 g/mol | EU-28 | agg | Sphera |
Isoprene (from C5 stream separation) from C5 stream separation ; single route, at plant ; 0.68 g/cm3, 68.12 g/mol | DE | agg | Sphera |
Isopropanol indirect hydrogenation ; single route, at plant ; 0.78 g/cm3, 60.10 g·/mol | BE | agg | Sphera |
Isopropanol (highly pure) isopropanol production by reacting propene in sulfuric acid, purification by distillation ; single route, at plant ; 0.78 g/cm3, 60.10 g/mol | US | agg | Sphera |
Isopropanolamine (by-product DIPA, TIPA) reaction of propylene oxide and ammonia ; production mix, at plant ; 0.97 g/cm3, 75.11 g/mol | DE | agg | Sphera |
Isopropanolamine (by-product MIPA, TIPA) reaction of propylene oxide and ammonia ; production mix, at plant ; 0.97 g/cm3, 75.11 g/mol | US | agg | Sphera |
Isopropylchloride reaction of hydrogen chloride and propene ; single route, at plant ; 0.86 g/cm3, 78.54 g/mol | DE | agg | Sphera |
Jatropha oil Jatropha cultivation, fruit harvest, transport, processing of seeds, oil extraction ; single route, at plant ; 37 MJ net calorific value | IN | agg | Sphera |
Jute cultivation (80% H2O content) jute cultivation ; production mix, at field border ; 80% H2O | BD | agg | Sphera |
Kaolin mining, wet processing, drying and grinding ; single route, at plant ; 2.16- 2.68 g/cm3 | CN | agg | Sphera |
Kaolin (extraction and processing) extraction and processing ; production mix, at plant ; 2.16- 2.68 g/cm3 | EU-28 | agg | Sphera |
Kerosene / Jet A1 at refinery from crude oil ; production mix, at refinery ; 400 ppm sulphur | NL | agg | Sphera |
Kerosene / Jet A1 at refinery from crude oil ; production mix, at refinery ; 0.2 wt.% sulphur | MY | agg | Sphera |
Kerosene / Jet A1 at refinery from crude oil ; production mix, at refinery ; 0.2 wt.% sulphur | RU | agg | Sphera |
Kerosene supplied and combusted [gasoline input in kg] (direct) Combustion of 1kg fuel input ; single route, at plant ; Scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Kerosene supplied and combusted [gasoline input in kg] (indirect) Combustion of 1kg fuel input ; single route, at plant ; Scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Kerosene supplied and combusted [Kerosene input in kg] Combustion of 1kg fuel input ; single route, at plant ; 44.1 MJ/kg net calorific value | EU-28 | agg | Sphera |
Kerosene supplied and combusted [th. energy output in MJ, 85% eta] Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; eta 85% | EU-28 | agg | Sphera |
Kerosene supplied and combusted [th. energy output in MJ, 85% eta] (direct) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; Scope 1 (direct GHG emissions) | EU-28 | agg | Sphera |
Kerosene supplied and combusted [th. energy output in MJ, 85% eta] (indirect) Combustion based on 1 MJ fuel input, eta 85%, thermal energy output 0,85 MJ ; single route, at plant ; Scope 3 (indirect GHG emissions) | EU-28 | agg | Sphera |
Kieselguhr calcined mining and calcination ; single route, at plant ; 80- 90% silica | EU-28 | agg | Sphera |
Kieselguhr calcined mining and calcination ; single route, at plant ; 80- 90% silica | DE | agg | Sphera |
Kraft paper (EN15804 A1-A3), wood input log hardwood technology mix ; production mix, at plant ; 1 kg | EU-28 | agg | Sphera |
Lactic acid (homofermentative) fermentation of carbohydrates ; single route, at plant ; 90.08 g/mol | DE | agg | Sphera |
Lactic acid (homofermentative) fermentation of carbohydrates ; single route, at plant ; 90.08 g/mol | EU-28 | agg | Sphera |
Lactic acid (homofermentative) - open input corn seeds fermentation of carbohydrates ; single route, at plant ; 90.08 g/mol | DE | p-agg | Sphera |
Lactose monohydrate (approximation) milk pretreatment, processing of curd and whey, ultrafiltration, reverse osmosis filtration, crystallisation, centrifugation, spray drying ; production mix, at plant ; 40% carbon content | DE | agg | Sphera |
L-alanine preparation (fermentation) (approximation) - open input energy, syrup and NaOH highly concentrated powder, via fermentation, estimation ; single route, at plant ; 1.42 g/cm3, 89.09 g/mol | CN | p-agg | Sphera |
Laminated gorilla glass (0.7 x 0.76 x 0.7 mm) batch meting, glass forming, annealing, chemical tempering and lamination ; single route, at plant ; 2.44 g/cm3, functional unit: 5.7 kg/sqm, Gorilla... | US | agg | Sphera |
Laminated tempered glass (1.6 x 0.76 x 1.6 mm) melting and forming, thermal tempering, lamination ; production mix, at plant ; 2.5 g/cm3, functional unit: 8.8 kg/sqm, Flat g... | EU-28 | agg | Sphera |
Landfilling of food waste (partially based on WARM data) treatment of leachate, production of electricity from percentage of landfill gas captured ; production mix (region specific sites), ... ; MSW, Municipal Solid Waste tre... | US | p-agg | Sphera |
Lanthan-Nickel5 (LaNi5, 88% lanthan, 12% nickel) mixing lanthan and nickel ; consumer mix, to consumer ; 88% lanthan, 12% nickel | EU-28 | agg | Sphera |
Lanthanum oxide primary production ; production mix, at plant ; RE95% | US | agg | Sphera |
Lanthanum oxide mix primary production ; production mix, at plant ; RE95% | GLO | agg | Sphera |
Latex ink - open input pigment latex ink for printing ; single route at producer ; average latex ink composition | EU-28 | p-agg | Sphera |
Laughing gas ammmonium nitrate route ; single route, at plant ; 1.85 kg/m3, 44.01 g/mol | DE | agg | Sphera |
Laurolactam from cyclododecanone ; single route, at plant ; 197.32 g/mol | DE | agg | Sphera |
Lauroyl chloride Chlorination of Lauric acid with Phosphorus trichloride ; single route, at plant ; molar mass: 218.5 g/mol, sum formula: C12H23ClO | EU-28 | agg | Sphera |
Lead battery 12V (approximation) assembling housing, electrodes and electrolyte ; production mix, at plant ; 12V | DE | agg | Sphera |
Lead oxide (Barton Pot, approximation) Barton Pot Process, oxidation of lead with air ; single route, at plant ; 9.53 g/cm3, 223.19 g/mol | EU-28 | agg | Sphera |
Lead stearate (stabilizer, approximation) reaction of stearic acid and lead oxide ; single producer, at plant ; 1.4 g/cm3, 774.15 g/mol | EU-28 | agg | Sphera |
Leather coating (PU) - open input leather spray coating of leather with polyurethane polyacrylate dispersion ; single route, at plant ; 1 kg of leather coated | EU-28 | p-agg | Sphera |
Leather finished painted, 1 kg - Chromium tanning (Wet Blue) Chromium tanning, finishing and painting ; production mix, at consumer ; 1 kg, average waste water | US | agg | Sphera |
Leather finished painted, 1 kg - Chromium tanning (Wet Blue) - open input cattle hide Chromium tanning, finishing and painting ; production mix, at consumer ; 1 kg, average waste water | US | p-agg | Sphera |
Leather finished unpainted, 1 kg - Chromium tanning (Wet Blue) Chromium tanning, after chromium tanning ; production mix, at consumer ; 1 kg, average waste water | US | agg | Sphera |
Leather hang drying (Split leather) - open input crust Hang drying ; single route, at plant ; 1 kg dried leather | EU-28 | p-agg | Sphera |
Leather retanning & finishing (aldehyde tanned; Split leather) - open input wet blue after aldehyde tanning ; single route, at plant ; 1 kg, average waste water | EU-28 | p-agg | Sphera |
Leather retanning & finishing (chromium tanned; Split leather) - open input wet blue Post-tanning/finishing after chrome tanning, average waste water emissions ; single route, at plant ; 1 kg | EU-28 | p-agg | Sphera |
Leather vacuum drying - open input wet blue leather vacuum drying ; single route, at plant ; 0.48% H2O for dried hide | EU-28 | p-agg | Sphera |
Leather vacuum drying - open input wet blue leather vacuum drying ; single route, at plant ; 0.48% H2O for dried hide | US | p-agg | Sphera |
Leather wet blue (Grain Split, Chromium tanning) - open input cattle hide Chromium tanning, average waste water treatment emissions ; single route, at plant ; 55% water content | EU-28 | p-agg | Sphera |
Leather wet white (Grain Split, Aldehyde tanning) - open input cattle hide Aldehyde tanning, average waste water treatment emissions ; single route, at plant ; 55% water content | EU-28 | p-agg | Sphera |
Light Fuel Oil (LFO) supplied and combusted in power plant technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 42.8 MJ/kg net calorific value | EU-28 | agg | Sphera |
Light Fuel Oil (LFO) supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 42.8 MJ/kg net calorific value | EU-28 | agg | Sphera |
Light Fuel Oil (LFO) supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning ; production mix, at heat plant ; 42.8 MJ/kg net calorific value | EU-28 | agg | Sphera |
Light fuel oil at refinery from crude oil ; production mix, at refinery ; 0.3 wt.% sulphur | RU | agg | Sphera |
Light fuel oil at refinery from crude oil ; production mix, at refinery ; 0.3 wt.% sulphur | MY | agg | Sphera |
Light fuel oil at refinery from crude oil ; production mix, at refinery ; 0.1 wt.% sulphur | NL | agg | Sphera |
Lignite dust drying and grinding lignite ; production mix, at plant ; 21.5 MJ net calorific value | EU-28 | agg | Sphera |
Lignite dust drying and grinding lignite ; production mix, at plant ; 21.5 MJ net calorific value | DE | agg | Sphera |
Lignite dust (approximation) drying and grinding lignite ; production mix, at plant ; 21.5 MJ net calorific value | IN | agg | Sphera |
Lime (CaO) grinding grinding ; production mix, at plant ; 3.34 g/cm3, 56.08 g/mol | EU-28 | agg | Sphera |
Lime (CaO) grinding grinding ; production mix, at plant ; 3.34 g/cm3, 56.08 g/mol | UA | agg | Sphera |
Lime (CaO) grinding grinding ; production mix, at plant ; 3.34 g/cm3, 56.08 g/mol | CN | agg | Sphera |
Lime (CaO) grinding grinding ; production mix, at plant ; 3.34 g/cm3, 56.08 g/mol | DE | agg | Sphera |
Lime (CaO; quicklime lumpy) from limestone ; production mix, at plant ; 3.37 g/cm3, 56.08 g/mol | MY | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | DE | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | UA | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | CN | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | NL | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | BR | agg | Sphera |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking ; production mix, at plant ; 2.24 g/cm3, 74.10 g/mol | EU-28 | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | EU-28 | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | AU | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | TH | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | BR | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | CN | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | NL | agg | Sphera |
Limestone (CaCO3; washed) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | UA | agg | Sphera |
Limestone (CaCO3; washed) (approximation) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | RU | agg | Sphera |
Limestone (CaCO3; washed) (approximation) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | GB | agg | Sphera |
Limestone (CaCO3; washed) (approximation) mining and benefication ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | IN | agg | Sphera |
Limestone flour (0.115mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.115mm | DE | agg | Sphera |
Limestone flour (0.115mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.115mm | EU-28 | agg | Sphera |
Limestone flour (0.12mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.12mm | EU-28 | agg | Sphera |
Limestone flour (0.12mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.12mm | DE | agg | Sphera |
Limestone flour (0.17mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.17mm | DE | agg | Sphera |
Limestone flour (0.17mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.17mm | EU-28 | agg | Sphera |
Limestone flour (0.1mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.1mm | EU-28 | agg | Sphera |
Limestone flour (0.25mm) limestone mining and milling ; production mix, at plant ; grain size 0.25mm | CN | agg | Sphera |
Limestone flour (0.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | DE | agg | Sphera |
Limestone flour (0.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | EU-28 | agg | Sphera |
Limestone flour (0.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | UA | agg | Sphera |
Limestone flour (0.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | BR | agg | Sphera |
Limestone flour (0.25mm) (approximation) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | TH | agg | Sphera |
Limestone flour (0.25mm) (approximation) limestone mining and beneficiation ; production mix, at plant ; grain size 0.25mm | RU | agg | Sphera |
Limestone flour (0.25mm) (approximation) limestone mining and milling ; production mix, at plant ; grain size 0.25mm | IN | agg | Sphera |
Limestone flour (0.25mm) (approximation) limestone mining and milling ; production mix, at plant ; grain size 0.25mm | BR | agg | Sphera |
Limestone flour (0.3mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.3mm | EU-28 | agg | Sphera |
Limestone flour (0.3mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.3mm | DE | agg | Sphera |
Limestone flour (0.5mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.5mm | EU-28 | agg | Sphera |
Limestone flour (0.75mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.75mm | DE | agg | Sphera |
Limestone flour (0.75mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.75mm | EU-28 | agg | Sphera |
Limestone flour (0.7mm) limestone mining and beneficiation ; production mix, at plant ; grain size 0.7mm | DE | agg | Sphera |
Limestone flour (0.7mm) limestone mining and beneficiation ; production mix, at producer ; grain size 0.7mm | EU-28 | agg | Sphera |
Limestone flour (1.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.25mm | DE | agg | Sphera |
Limestone flour (1.25mm) limestone mining and beneficiation ; production mix, at producer ; grain size 1.25mm | EU-28 | agg | Sphera |
Limestone flour (1.75mm) limestone mining and beneficiation ; production mix, at producer ; grain size 1.75mm | EU-28 | agg | Sphera |
Limestone flour (1.75mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.75mm | DE | agg | Sphera |
Limestone flour (1.82mm) limestone mining and beneficiation ; production mix, at producer ; grain size 1.82mm | EU-28 | agg | Sphera |
Limestone flour (1.82mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.82mm | DE | agg | Sphera |
Limestone flour (12µm) limestone mining and beneficiation ; production mix, at producer ; grain size 12µm | EU-28 | agg | Sphera |
Limestone flour (12µm) limestone mining and beneficiation ; production mix, at plant ; grain size 12µm | DE | agg | Sphera |
Limestone flour (2.15mm) limestone mining and beneficiation ; production mix, at plant ; grain size 2.15mm | DE | agg | Sphera |
Limestone flour (2.15mm) limestone mining and beneficiation ; production mix, at producer ; grain size 2.15mm | EU-28 | agg | Sphera |
Limestone flour (2.25mm) limestone mining and beneficiation ; production mix, at producer ; grain size 2.25mm | EU-28 | agg | Sphera |
Limestone flour (2.25mm) limestone mining and beneficiation ; production mix, at plant ; grain size 2.25mm | DE | agg | Sphera |
Limestone flour (25µm) limestone mining and beneficiation ; production mix, at producer ; grain size 25µm | EU-28 | agg | Sphera |
Limestone flour (25µm) limestone mining and beneficiation ; production mix, at plant ; grain size 25µm | DE | agg | Sphera |
Limestone flour (29µm) limestone mining and beneficiation ; production mix, at producer ; grain size 29µm | EU-28 | agg | Sphera |
Limestone flour (29µm) limestone mining and beneficiation ; production mix, at plant ; grain size 29µm | DE | agg | Sphera |
Limestone flour (30µm) limestone mining and beneficiation ; production mix, at plant ; grain size 30µm | DE | agg | Sphera |
Limestone flour (30µm) limestone mining and beneficiation ; production mix, at producer ; grain size 30µm | EU-28 | agg | Sphera |
Limestone flour (46µm) limestone mining and beneficiation ; production mix, at plant ; grain size 46µm | DE | agg | Sphera |
Limestone flour (46µm) limestone mining and beneficiation ; production mix, at producer ; grain size 46µm | EU-28 | agg | Sphera |
Limestone flour (50µm) limestone mining and beneficiation ; production mix, at producer ; grain size 50µm | EU-28 | agg | Sphera |
Limestone flour (7µm) limestone mining and beneficiation ; production mix, at plant ; grain size 7µm | DE | agg | Sphera |
Limestone flour (7µm) limestone mining and beneficiation ; production mix, at producer ; grain size 7µm | EU-28 | agg | Sphera |
Limestone flour (CaCO3; dried) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | UA | agg | Sphera |
Limestone flour (CaCO3; dried) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | EU-28 | agg | Sphera |
Limestone flour (CaCO3; dried) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | BR | agg | Sphera |
Limestone flour (CaCO3; dried) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | AU | agg | Sphera |
Limestone flour (CaCO3; dried) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | CN | agg | Sphera |
Limestone flour (CaCO3; dried) (approximation) milling and drying ; production mix, at plant ; 2.73 g/cm3, 100.09 g/mol | IN | agg | Sphera |
Linoleic acid from rape oil (by-product other fatty acids) enzymatic hydrolysis and distillation ; production mix, at plant ; 0.90 g/cm3, 280.45 g/mol | DE | agg | Sphera |
Linolen acid from rape oil (by-product other fatty acids) enzymatic hydrolysis and distillation ; production mix, at plant ; 0.90 g/cm3, 280.45 g/mol | DE | agg | Sphera |
LiPF6 - EC - DMC electrolyte for Li-ion battery from dimethyl carbonate, ethylene carbonate and lithium hexafluorophosphate ; single route, at producer | DE | agg | Sphera |
Liquefied natural gas (LNG) technology mix (large scale) ; production mix, at storage terminal ; 48.9 MJ/kg net calorific value | US | agg | Sphera |
Liquefied natural gas (LNG) mix technology mix ; consumption mix, to consumer ; medium pressure level (< 1 bar) | EU-28 | agg | Sphera |
Liquefied Petroleum Gas (LPG) from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | AU | agg | Sphera |
Liquefied Petroleum Gas (LPG) from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | EU-28 | agg | Sphera |
Liquefied Petroleum Gas (LPG) from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | RO | agg | Sphera |
Liquefied Petroleum Gas (LPG) from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | GB | agg | Sphera |
Liquefied Petroleum Gas (LPG) from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | NL | agg | Sphera |
Liquefied Petroleum Gas (LPG), from conventional natural gas production from conventional natural gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | US | agg | Sphera |
Liquefied Petroleum Gas (LPG), from shale gas production from shale gas production ; production mix, at producer ; 46.16 MJ/kg net calorific value | US | agg | Sphera |
Liquid carbon dioxide electric- driven compression of gaseous carbon dioxide ; production mix, at plant ; 60 bar pressure | US | agg | Sphera |
Liquid Crystal Display (LCD), Panel Assembly LED TFT, mixed TN-IPS technology (mobile phone), in sqm TN-IPS technology, without LCD controller, without glass overlay ; production mix, at plant ; in sqm | GLO | agg | Sphera |
Liquid Crystalline Polymer without glass fiber (LCP) acidolysis of 4- hydroxybenzoic acid (HBA) with 6-hydroxy-2- naphthoic acid (HNA) ; single producer at plant ; LCP without glass fiber | US | agg | Sphera |
Liquidcrystalline Polymer with 30% glass fiber (LCP) acidolysis of 4- hydroxybenzoic acid (HBA) with 6-hydroxy-2- naphthoic acid (HNA) ; single producer at plant ; LCP GF 30 | DE | agg | Sphera |
Liquidcrystalline polymer without glass fiber (LCP) acidolysis of 4- hydroxybenzoic acid (HBA) with 6-hydroxy-2- naphthoic acid (HNA) ; single producer at plant ; LCP without glass fiber | DE | agg | Sphera |
Lithium bromide 46% solution (approximation) Reaction of lithium hydroxide with hydrobromic acid ; single route, at producer ; 46% solution | DE | agg | Sphera |
Lithium carbonate (from brine) extraction from brine ; production mix, at plant ; 2.11 g/cm3, 73.89 g/mol | CL | agg | Sphera |
Lithium carbonate (spodumene route) (with credits) spodumene route ; production mix, at plant ; battery grade Li2CO3 (99.9 % purity) | CN | agg | Sphera |
Lithium carbonate (Spodumene) (price allocated) spodumene route ; production mix, at plant ; battery grade Li2CO3 (99.9 % purity) | AU | agg | Sphera |
Lithium Carbonate mix technology mix ; production mix, at plant ; 2.11 g/cm3, 73.89 g/mol | GLO | agg | Sphera |
Lithium carbonate mix (brine) extraction from brine ; production mix, at plant ; 2.11 g/cm3, 73.89 g/mol | GLO | agg | Sphera |
Lithium carbonate mix (spodumene) spodumene route ; production mix, at plant ; 2.11 g/cm3, 73.89 g/mol | GLO | agg | Sphera |
Lithium carbonate Spodumene Route (price allocated) spodumene route ; production mix, at plant ; battery grade Li2CO3 (99.9 % purity) | CN | agg | Sphera |
Lithium chloride (from lithium carbonate) reaction of hydrogen chloride and lithium carbonate ; single route, at plant ; 2.07 g/cm3, 42.39 g/mol | DE | agg | Sphera |
Lithium chloride (from lithium hydroxide) reaction of hydrogen chloride and lithium hydroxide ; single route, at plant ; 2.07 g/cm3, 42.39 g/mol | DE | agg | Sphera |
Lithium chloride (from lithium hydroxide) reaction of hydrogen chloride and lithium carbonate ; single route, at plant ; 2.07 g/cm3, 42.39 g/mol | US | agg | Sphera |
Lithium fluoride reaction of lithium hydroxide and hydrogen fluoride ; single route, at plant ; 2.64 g/cm3, 25.94 g/mol | JP | agg | Sphera |
Lithium Hexafluorophosphate (LiPF6) reaction of lithium fluoride and phosphorous pentafluoride ; production mix, at plant ; 1.5 g/cm3, 151.9 g/mol | JP | agg | Sphera |
Lithium hydroxide reaction between lithium carbonate and calcium hydroxide ; production mix, at plant ; 1.46 g/cm3, 23.95 g/mol | CN | agg | Sphera |
Lithium hydroxide reaction between lithium carbonate and calcium hydroxide ; production mix, at plant ; 1.46 g/cm3, 23.95 g/mol | JP | agg | Sphera |
Lithium hydroxide reaction between lithium carbonate and calcium hydroxide ; production mix, at plant ; 1.46 g/cm3, 23.95 g/mol | EU-28 | agg | Sphera |
Lithium hydroxide reaction between lithium carbonate and calcium hydroxide ; production mix, at plant ; 1.46 g/cm3, 23.95 g/mol | DE | agg | Sphera |
Lithium hydroxide digestion of spodumene with lime ; single route, at plant ; 1.46 g/cm3, 23.95 g/mol | US | agg | Sphera |
Lithium hydroxide - open input lithium carbonate digestion of spodumene with lime ; single route, at plant ; 1.46 g/cm3, 23.95 g/mol | DE | p-agg | Sphera |
Lithium manganese oxide sintering lithium carbonate and manganous oxide ; production mix, at plant ; 2.93 g/cm3 | JP | agg | Sphera |
Lithium metal (high Na-concentration) electrolysis of lithium chloride (LiCl) ; single route, at plant ; 0.534 g/cm3, 6.94 g/mol | DE | agg | Sphera |
Lithium metal (low Na-concentration) electrolysis of lithium chloride (LiCl) ; single route, at plant ; 0.534 g/cm3, 6.94 g/mol | US | agg | Sphera |
Lithium metal (low Na-concentration) electrolysis of lithium chloride (LiCl) ; single route, at plant ; 0.534 g/cm3, 6.94 g/mol | DE | agg | Sphera |
Lithium nickel cobalt manganese oxide battery pack (NMC 622), 100 kg - open input housing production of battery components, battery assembling ; single route, at plant ; battery weight 100 kg, housing weight 13 kg, cap... | CN | p-agg | Sphera |
Lithium phosphate from lithium hydroxide and phosphoric acid ; single route, at plant ; 2.41 g/cm3, 115.79 g/mol | DE | agg | Sphera |
Lithium sulfide from lithium hydroxide (approximation) from reaction of lithium hydroxide with hydrogen sulfide ; single route, at producer ; 45.95 g/mol | DE | agg | Sphera |
Lithium sulfide from lithium hydroxide (approximation) from reaction of lithium hydroxide with hydrogen sulfide ; single route, at producer ; 45.95 g/mol | JP | agg | Sphera |
Lithium sulfide from lithium metal (approximation) from reaction of lithium metal with sulfur ; single route, at producer ; 45.95 g/mol | JP | agg | Sphera |
Lithium sulfide from lithium metal (approximation) from reaction of lithium metal with sulfur ; single route, at producer ; 45.95 g/mol | DE | agg | Sphera |
Lithium sulfide from lithium sulphate and carbon black (approximation) from reaction of lithium sulphate with carbon black ; single route, at producer ; 45.95 g/mol | EU-28 | agg | Sphera |
Lithium sulphide from lithium carbonate and hydrogen sulphide (approximation) from reaction of lithium carbonate with hydrogen sulfide ; single route, at producer ; 45.95 g/mol | EU-28 | agg | Sphera |
Lithium titanate (Li4Ti5O12) technology mix, sol gel method and hydrothermal synthesis ; production mix, at plant ; 459 g/mol | GLO | agg | Sphera |
Lithium titanate (Li4Ti5O12) from titanium oxichloride and lithium carbonate Sol gel method, from lithium carbonate and titanium tetrachloride ; Single route, at plant ; 459 g/mol | GLO | agg | Sphera |
Lithium titanate (Li4Ti5O12) from titanium(IV) isopropoxide (TTIP) Hydrothermal synthesis, from lithium ethanolate and titanium isopropoxide ; Single route, at plant ; 459 g/mol | GLO | agg | Sphera |
Lithium-ion LCO (LiCoO2) battery cell, 100g production of battery components, battery assembling ; single route, at plant ; energy density of cell: 220 Wh/kg | CN | agg | Sphera |
Lithium-ion LCO (LiCoO2) battery cell, 1kg production of battery components, battery assembling ; single route, at plant ; energy density of cell: 220 Wh/kg | CN | agg | Sphera |
Lithium-ion LFP (LiFePO4) battery cell, 162 Wh/kg energy density, 100g production of battery components, battery assembling ; single route, at plant ; energy density of cell: 162 Wh/kg | CN | agg | Sphera |
Lithium-ion LFP (LiFePO4) battery cell, 162 Wh/kg energy density, 1kg battery cell production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion LFP (LiFePO4) battery cell, 162 Wh/kg energy density, 1kWh battery cell production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion LFP battery pack incl. periphery, 20 kWh, 190 kg battery cell, module and pack production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion LFP battery pack incl. periphery, 40 kWh, 330 kg battery cell, module and pack production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion LFP battery pack incl. periphery, 60 kWh, 470 kg battery cell, module and pack production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion LFP battery pack incl. periphery, 80 kWh, 611 kg battery cell, module and pack production ; single route, at producer ; energy density: 162 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery cell, 226 Wh/kg energy density, 1kg battery cell production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery cell, 226 Wh/kg energy density, 1kWh battery cell production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery pack incl. periphery, 20 kWh, 140 kg battery cell, module and pack production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery pack incl. periphery, 40 kWh, 242 kg battery cell, module and pack production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery pack incl. periphery, 60 kWh, 343 kg battery cell, module and pack production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NCA battery pack incl. periphery, 80 kWh, 444 kg battery cell, module and pack production ; single route, at producer ; energy density: 226 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery cell, 220 Wh/kg energy density, 100g production of battery components, battery assembling ; single route, at plant ; energy density of cell: 220 Wh/kg | CN | agg | Sphera |
Lithium-ion NMC 622 battery cell, 220 Wh/kg energy density, 1kg battery cell production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery cell, 220 Wh/kg energy density, 1kWh battery cell production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery cell, 220 Wh/kg energy density, 40g production of battery components, battery assembling ; single route, at plant ; energy density of cell: 220 Wh/kg | DE | agg | Sphera |
Lithium-ion NMC 622 battery pack incl. periphery, 20 kWh, 142 kg battery cell, module and pack production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery pack incl. periphery, 40 kWh, 246 kg battery cell, module and pack production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery pack incl. periphery, 60 kWh, 350 kg battery cell, module and pack production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Lithium-ion NMC 622 battery pack incl. periphery, 80 kWh, 455 kg battery cell, module and pack production ; single route, at producer ; energy density: 220 Wh/kg cell, cathode activ... | CN | agg | Sphera |
Log hardwood mix (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 50% timber beech, 50% timber oak, 0 % moisture... | EU-28 | agg | Sphera |
Log hardwood mix (0 % moisture, 0% H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 50% timber beech, 50% timber oak, 0 % moisture... | DE | agg | Sphera |
Log hardwood mix (25 % moisture content, 20 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 75% timber beech, 25% timber oak, 25 % moistur... | EU-28 | agg | Sphera |
Log softwood mix (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 50% timber spruce, 50% timber pine - 0 % mois... | EU-28 | agg | Sphera |
Log softwood mix (0 % moisture content, 0 % H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 100% timber spruce, 0 % moisture content / 0 %... | DE | agg | Sphera |
Log softwood mix (25% moisture content, 20% H2O content) forest cultivation, harvesting, wet storage ; production mix, at plant ; 20% H2O, 35% timber spruce, 65% timber pine, 2... | EU-28 | agg | Sphera |
Low density polyethylene foil (LDPE foil) PE extruding, melting, casting and mechanical forming ; single route, at plant ; 0.91- 0.96 g/cm3 | BE | agg | Sphera |
L-sorbose preparation microbial oxidation of sorbitol ; production mix, at plant ; 1.65 g/cm3, 180.16 g/mol | US | agg | Sphera |
Lubricants at refinery from crude oil ; production mix, at refinery ; 38 MJ/kg net calorific value | NL | agg | Sphera |
Lubricants at refinery from crude oil ; production mix, at refinery ; 38 MJ/kg net calorific value | RU | agg | Sphera |
Magnesium acetate from lime and formic acid ; single route, at plant ; 1.45 g/cm3, 142.39 g/mol | DE | agg | Sphera |
Magnesium carbonate (MgCO3, fine, washed for fillers) mining, milling, sifting ; production mix, at plant ; 2.96 g/cm3, 84.31 g/mol | EU-28 | agg | Sphera |
Magnesium carbonate (MgCO3, finely, washed for fillers) mining, milling, sifting ; production mix, at plant ; 2.96 g/cm3, 84.31 g/mol | DE | agg | Sphera |
Magnesium Hydroxide (from sea water) from brine ; single route, at plant ; 2.34 g/cm3, 58.32 g/mol | EU-28 | agg | Sphera |
Magnesium oxide (MgO, calcinate, fillers) Dolomite preparation, calcination ; single route, at plant ; 3.58 g/cm3, 40.30 g/mol | DE | agg | Sphera |
Magnesium oxide (MgO, calcinate, fillers) Dolomite preparation, calcination ; single route, at plant ; 3.58 g/cm3, 40.30 g/mol | EU-28 | agg | Sphera |
Magnesium oxide (MgO, fine, filler) calcining magnesium carbonate ; single route, at plant ; 3.58 g/cm3, 40.30 g/mol | EU-28 | agg | Sphera |
Magnesium oxide (MgO, fine, filler) calcining magnesium carbonate ; single route, at plant ; 3.58 g/cm3, 40.30 g/mol | DE | agg | Sphera |
Magnesium sulfate (50% in water) technology mix ; production mix, at plant ; MgSO4 | EU-28 | agg | Sphera |
Magnesium sulphate (agrarian) (economic allocation) from carnallitic hard salt ; single route, at plant ; 2.66 g/cm3, 120.366 g/mol | EU-28 | agg | Sphera |
Magnet Nd-Fe-Dy-B sintered magnet process ; single route, at plant ; energy density >385 kJ/m³, composition: 1% boron... | CN | agg | Sphera |
Magnet Nd-Fe-Dy-B sintered magnet process ; single route, at plant ; energy density >385 kJ/m³, composition: 1% boron... | DE | agg | Sphera |
Maize cultivation, whole plant (72.6% H2O content) technology mix ; production mix, at field border ; 72.6% H2O | DE | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | US | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | DE | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | IT | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | GB | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | NL | agg | Sphera |
Maleic anhydride (MA) by-product phthalic anhydride (by oxidation of xylene) oxidation of xylene ; single route, at plant ; 1.48 g/cm3, 98.06 g/mol | FR | agg | Sphera |
Manganese chloride (from chlorination of Mn) chlorination of manganese ; single route, at plant ; 2.99 g/cm3, 125.844 g/mol | DE | agg | Sphera |
Manganese monoxide (MnO) mining, beneficiation, concentration ; production mix, at plant ; 5.43 g/cm3, 70.94 g/mol | ZA | agg | Sphera |
Manganese monoxide, highly pure (MnO) mining, beneficiation, concentration, electrolysis ; production mix, at plant ; 5.43 g/cm3, 70.94 g/mol | ZA | agg | Sphera |
Manganese sulphate (approximation) manganese dissolved in sulphuric acid ; single route, at plant ; 3.25 g/cm3, 151.00 g/mol | DE | agg | Sphera |
Manganese-chloride-mix (50% direct chlorination of Mn; 50% reaction of HCL (aq.) with MnO) 50% direct chlorination of Mn; 50% reaction of HCL (aq.) with MnO ; single route, at producer ; 2.98 g/cm3, 125.84 g/mol | DE | agg | Sphera |
Manufacturing electric motor (<=10kW) assembling electric motor ; production mix, at plant ; <=10kW | EU-28 | agg | Sphera |
Manufacturing electric motor (101-200kW) combination of steel, cast iron, copper, aluminium, impregnation resin and insulation material ; production mix, at plant ; 101-200kW | EU-28 | agg | Sphera |
Manufacturing electric motor (11-100kW) combination of steel, cast iron, copper, aluminium, impregnation resin and insulation material ; production mix, at plant ; 11-100kW | EU-28 | agg | Sphera |
Marble (granulation 1.5-2.5 mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.5-2.5 mm | CN | agg | Sphera |
Marble (granulation 1.5-2.5 mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.5-2.5 mm | UA | agg | Sphera |
Marble (granulation 1.5-2.5 mm) limestone mining and beneficiation ; production mix, at plant ; grain size 1.5-2.5 mm | DE | agg | Sphera |
Marble (granulation 30 µm) limestone mining and beneficiation ; production mix, at plant ; grain size 30 µm | UA | agg | Sphera |
Marble (granulation 30 µm) limestone mining and beneficiation ; production mix, at plant ; grain size 30 µm | CN | agg | Sphera |
Marble (granulation 30 µm) limestone mining and beneficiation ; production mix, at plant ; grain size 30 µm | DE | agg | Sphera |
Meal - including meat (average) freshly made canteen food (electric stove) ; consumption mix, to consumer ; 735 kcal per meal, 453.5g per meal (weight... | GLO | agg | Sphera |
Meal - vegan (average) freshly made canteen food (electric stove) ; consumption mix, to consumer ; 735 kcal per meal, 698.8g per meal (weight... | GLO | agg | Sphera |
Meal - vegetarian (average) freshly made canteen food (electric stove) ; consumption mix, to consumer ; 735 kcal per meal, 737.3g per meal (weight... | GLO | agg | Sphera |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | US | agg | Sphera |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | BR | agg | Sphera |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | NZ | agg | Sphera |
Meat and bone meal (MBM) from pig (economic allocation) (approximation) slaughtering and processing ; single route, at plant ; product specification (such as energy, protein a... | RU | agg | Sphera |
Melamin urea formaldehyde (MUF) adhesive system (20% H2O) hydromethylation and condensation reactions of melamine, urea and formaldehyde ; single route, at plant ; 20% H2O | US | agg | Sphera |
Melamine (Stami carbon process) Stami carbon process ; production mix, at plant ; 1574 kg/m3, 126 g/mol | US | agg | Sphera |
Melamine foam melamine- formaldehyde addition, etherification with alcohol (foaming) ; single route, at plant ; 14 MJ/ kg net calorific value | DE | agg | Sphera |
Metal Glue (Screw sealing) components mixing ; single route, at plant ; 20% succinic acid dibutyl ester, 70% glycidylmet... | EU-28 | agg | Sphera |
Methacrylate Esterification of Acrylic acid with methanol ; single route, at producer ; Colorless, 950 kg/m³ | IT | agg | Sphera |
Methacrylate Esterification of Acrylic acid with methanol ; single route, at producer ; Colorless, 950 kg/m³ | BE | agg | Sphera |
Methacrylate Esterification of Acrylic acid with methanol ; single route, at producer ; Colorless, 950 kg/m³ | FR | agg | Sphera |
Methacrylate Esterification of Acrylic acid with methanol ; single route, at producer ; Colorless, 950 kg/m³ | GB | agg | Sphera |
Methacrylate Esterification of Acrylic acid with methanol ; single route, at producer ; Colorless, 950 kg/m³ | NL | agg | Sphera |
Methacrylic acid over isobutyric acid ; single route, at plant ; 1.02 g/cm3, 86.06 g/mol | EU-28 | agg | Sphera |
Methacrylic acid over isobutyric acid ; single route, at plant ; 1.02 g/cm3, 86.06 g/mol | DE | agg | Sphera |
Methacrylonitrile (approximation) Sohio process (ammoxidation) ; single route at producer ; 67,09 g/mol | EU-28 | agg | Sphera |
Methane (from natural gas) purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | AU | agg | Sphera |
Methane (from natural gas) purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | SA | agg | Sphera |
Methane (from refinery gas separation) from crude oil ; production mix, at refinery ; 50 MJ/kg net calorific value | DE | agg | Sphera |
Methanol from coal via coal gasification, integrated power plant, without carbon capture ; single route, at plant ; 0.79 g/cm3, 32.04 g/mol | CN | agg | Sphera |
Methanol from natural gas from natural gas ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | GB | agg | Sphera |
Methanol from natural gas from natural gas ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | IT | agg | Sphera |
Methanol from natural gas from natural gas ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | NL | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | OM | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | EG | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol, 19.93 MJ/kg | TT | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | SA | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | RU | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | VE | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | JP | agg | Sphera |
Methanol from natural gas (combined reforming) from natural gas ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | NO | agg | Sphera |
Methanol from natural gas (combined reforming) approximation from natural gas, combined reforming ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | CN | agg | Sphera |
Methanol from natural gas (integrated technology) from natural gas, integrated technology ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | MY | agg | Sphera |
Methanthiol (methyl mercaptan) reaction of methanol and hydrogen sulphide ; production mix, at plant ; 2.00 kg/m3, 48.11 g/mol | EU-28 | agg | Sphera |
Methanthiol (methyl mercaptan) reaction of methanol and hydrogen sulphide ; production mix, at plant ; 2.00 kg/m3, 48.11 g/mol | DE | agg | Sphera |
Methionine from ammonia ; single route, at plant ; 149.21 g/mol | US | agg | Sphera |
Methionine from ammonia ; single route, at plant ; 149.21 g/mol | BR | agg | Sphera |
Methoxypropylacetate PGMEA (approximation) esterification of propylene glycol monomethyl ether with acetic acid ; production mix, at plant ; 0.96 g/cm³, 132.2 g/mol | DE | agg | Sphera |
Methyl acrylate from acrylic acid by esterification esterification of acrylic acid and methanol ; single route, at plant ; 0.95 g/cm³, 86.09 g/ mol | DE | agg | Sphera |
Methyl cellulose via alkali cellulose ; production mix, at plant ; 0.25- 0.7 g/cm3 | DE | agg | Sphera |
Methyl chloroformate esterification of methanol and chloroform ; single route, at plant ; 1.22 g/mL, 94.49 g/mol | DE | agg | Sphera |
Methyl dichlorosilane by-product chlorosilane reaction of silicon and methyl chloride ; single route, at plant ; 1.10 g/cm3, 114.02 g/mol | DE | agg | Sphera |
Methyl ethyl ketone (2-butanone, MEK) via methyl-t-butylether ; production mix, at plant ; 0.805 g/cm3, 72.11 g/mol | DE | agg | Sphera |
Methyl isobutyl ketone (MIBK) from acetone and hydrogen ; single route, at plant ; 0.80 g/cm3, 100.16 g/mol | EU-28 | agg | Sphera |
Methyl isocyanate amine phosgenation ; single producer, at plant ; 0.96 g/cm3, 57.05 g/mol | DE | agg | Sphera |
Methyl mercaptan reaction of methanol and hydrogen sulphide ; production mix, at plant ; 2.00 kg/m3, 48.11 g/mol | DE | agg | Sphera |
Methyl methacrylate (MMA) (technology mix) technology mix ; production mix, at plant ; 0.94 g/cm³, 100 g/mol | DE | agg | Sphera |
Methyl styrene by-product phenol, acetone (from Cumene) Hock Process, oxidation of cumene ; production mix, at plant ; 0.91 g/cm3, 118.18 g/mol | DE | agg | Sphera |
Methyl trichlorosilane by-product chlorosilanes Rochow- Müller- Synthesis ; production mix, at plant ; 1.34 g/cm3, 135.45 g/mol | DE | agg | Sphera |
Methylamine (by-product di-, trimethylamine) via methanol and ammonia ; production mix, at plant ; 31.06 g/mol, 30.87 MJ/kg net calorific value | EU-28 | agg | Sphera |
Methylamine by-product di-, trimethylamine via methanol and ammonia ; production mix, at plant ; 31.06 g/mol | DE | agg | Sphera |
Methyldiethanolamine (MDEA) reaction of ethylene oxide and monomethylamine ; production mix, at plant ; 1.04 g/cm3, 119.16 g/mol | DE | agg | Sphera |
Methylendianiline (MDA) by-product polymethylene polyphenylamine via aniline hydrogenation of the benzene ; production mix, at plant ; 1.05 g/cm3, 198.27 g/mol | DE | agg | Sphera |
Methylene diphenyl diisocyanate (MDI) by-product hydrochloric acid, methanol phosgenation of methylenedianiline ; production mix, at plant ; 1.23 g/cm3, 250 g/mol | CN | agg | Sphera |
Methylmethacrylate (MMA, recycling of spent acid) recycling of spent acid ; production mix, at plant ; 0.94 g/cm³, 100.12 g/mol | EU-28 | agg | Sphera |
Methylstyrene by-product acetone, phenol (from cumene) Hock Process, oxidation of cumene ; production mix, at plant ; 0.91 g/cm3, 118.18 g/mol | US | agg | Sphera |
Methyl-t-Butylether (MTBE) by-product C4 raffinate of C4 cut etherification of isobutylene with methanol ; single route, at plant ; 0.74 g/cm3, 88.15 g/mol | DE | agg | Sphera |
Methyl-t-Butylether (MTBE) by-product Isobutene of C4 raffinate with n-butene Isomerisation acid-catalyzed addition of methanol to isobutene ; production mix, at plant ; 0.74 g/cm³, C5H12O | CN | agg | Sphera |
Methyl-t-Butylether (MTBE) by-product Isobutene of C4 raffinate with n-butene Isomerisation acid-catalyzed addition of methanol to isobutene ; production mix, at plant ; 0.74 g/cm³, C5H12O | DE | agg | Sphera |
Microsilica/Silica fume, by-product ferro silicon by-product from production of ferro-silicon ; production mix, at plant ; 90% concentration | NO | agg | Sphera |
Microsilica/Silica fume, by-product ferro silicon by-product from production of ferro-silicon ; production mix, at plant ; 90% concentration | RU | agg | Sphera |
Milk protein concentrate powder (from skim milk) (MPC 70) via spray drying ; production mix, at producer ; MPC 70 | US | agg | Sphera |
Milk protein concentrate powder (from skim milk) (MPC 70) (4% moisture, 1% fat) via spray drying ; production mix, at producer ; MPC 70 | US | agg | Sphera |
Milk protein concentrate powder (from skim milk) (MPC 70) (fat allocation) via spray drying ; production mix, at producer ; MPC 70 | US | agg | Sphera |
Milk protein concentrate powder 4424 (MPC 70) via spray drying ; production mix, at producer ; MPC 4424 | US | agg | Sphera |
Milk protein concentrate powder 4424 (MPC) (3% moisture, 26.4% fat) via spray drying ; production mix, at producer ; MPC 4424, 3% moisture, 26.4% fat | US | agg | Sphera |
Mobile phone Production of a generic mobile phone ; production mix, at plant ; 140 g, 5" Display, Lithium-polymer | GLO | p-agg | Sphera |
Molasse from sugar beet washing, shredding, extraction, sterilization, juice purification and concentration, crystallization ; production mix, at plant ; beet molasses, 20% H2O | EU-28 | agg | Sphera |
Molasse from sugar cane by-product from crystall sugar production ; single route, at plant ; 20% H2O | TH | agg | Sphera |
Molasse from sugar cane (45% burning) by-product from crystall sugar production ; single route, at plant ; 20% H2O | BR | agg | Sphera |
Molded pulp loose from bagasse integrated plant case (approximation) pulp blending, molding, drying ; single route, at plant ; energy for the process from bagasse combustion | CN | agg | Sphera |
Molded pulp loose from bagasse stand alone plant case (approximation) pulp blending, molding, drying ; single route, at plant ; energy for the process from natural gas and elec... | CN | agg | Sphera |
Molybdenum flotation, roasting, reduction ; production mix, at plant ; 10.28 g/cm3 | GLO | agg | Sphera |
Molybdenum trioxide (technical-grade MoO3) Primary production, mining and processing ; production mix, at plant ; tech oxide | GLO | agg | Sphera |
Monocalciumphosphate (MCP; for Feed) (approximation) from burnt chalk and phosphoric acid ; single route, at plant ; 252.05 g/mol | EU-28 | agg | Sphera |
Monocalciumphosphate (MCP; for Feed) (approximation) from burnt chalk and phosphoric acid ; single route, at plant ; 252.05 g/mol | GLO | agg | Sphera |
Monoethanolamine (MEA) by-prod. ethanolamines from ethylene oxide ; production mix, at plant ; 1.01 g/cm3, 61.08 g/mol | US | agg | Sphera |
Monoethanolamine (MEA) by-prod. ethanolamines from ethylene oxide ; production mix, at plant ; 1.01 g/cm3, 61.08 g/mol | EU-28 | agg | Sphera |
Monoethanolamine (MEA) by-prod. ethanolamines from ethylene oxide ; production mix, at plant ; 1.01 g/cm3, 61.08 g/mol | DE | agg | Sphera |
Monoethanolamine 99% (1% aq.) (MEA) by-prod. ethanolamines from ethylene oxide ; production mix, at plant ; 1.01 g/cm3, 61.08 g/mol | US | agg | Sphera |
Mono-Methylethanolamine (MMA) reaction of ethylene oxide with methyl amine ; single route, at plant ; 0.935 g/mL, 75.11 g/mol | DE | agg | Sphera |
Monosodium phosphate leaching, ore pretreatment and neutralization ; single route, at plant ; 2.36 g/cm3, 119.98 g/mol | US | agg | Sphera |
Mozzarella manufacturing curd product |