1,1,1-Trichloroethane (methylchloroform) chlorination of ethane; production mix, at plant; 1.34 g/cm3, 133.42 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
1,3-Butadiene oxidative catalytic dehydrogenation of C4; production mix, at plant; 2.4982 kg/m3, 54.09 g/mol | NL | agg | ts |
1,3-Butadiene oxidative catalytic dehydrogenation of C4; production mix, at plant; 2.4982 kg/m3, 54.09 g/mol | ES | agg | ts |
1,3-Butadiene oxidative catalytic dehydrogenation of C4; production mix, at plant; 2.4982 kg/m3, 54.09 g/mol | CN | agg | ts |
1,3-Butadiene oxidative catalytic dehydrogenation of C4; production mix, at plant; 2.4982 kg/m3, 54.09 g/mol | JP | agg | ts |
1,3-butadiene oxidative catalytic dehydrogenation of C4; production mix, at plant; 2.4982 kg/m3, 54.09 g/mol | NO | agg | ts |
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 | ts |
1,6-Hexanediol (estimation) catalytic hydrogenation of adipic acid; production mix, at plant; 118.18 g/mol | EU-28 | agg | ts |
1,6-Hexanediol (estimation) catalytic hydrogenation of adipic acid; single producer, at plant; 118.18 g/mol | DE | agg | ts |
1-Aminoanthraquinone from chlorobenzoic acid and xylene; production mix, at plant; 223.23 g/mol | US | agg | ts |
1-Decanol (estmation) Hydrogenation of decanoic acid, based on palm kernel oil; production mix, at plant; 0.8297 g/cm3, 158.28 g/mol | EU-28 | agg | ts |
1-Decene by-product Linear Alphaolefine (LAO) (mass allocation) (estimation) oligomerization of ethylene, by-product Linear Alphaolefine; single route, at plant; 0.74 g/cm3, 140.27 g/mol | DE | agg | ts |
1-Dodecanol hydrogenation of dodecanoic acid; production mix, at plant; 0.83 g/cm3, 186.34 g/mol | DE | agg | ts |
1-Dodecanol hydrogenation of dodecanoic acid; production mix, at plant; 0.83 g/cm3, 186.34 g/mol | EU-28 | agg | ts |
2-(Perfluorohexyl)ethyl iodide radical-catalysed addition of ethylene to perfluorohexyl iodide; single route, at producer; 474 g/mol | US | agg | ts |
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/mol | DE | agg | ts |
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/mol | EU-28 | agg | ts |
2-Dimethylaminoethanol (DMAE) reaction of dimethylamine and ethylene oxide; production mix, at plant; 0.89 g/cm3, 89.14 g/mol | EU-28 | agg | ts |
2-Ethylhexanol from propylene Aldolization of butyraldehyde; production mix, at plant; 0.83 g/cm3, 130.23 g/mol | US | agg | ts |
2-Ethylhexanol from propylene Aldolization of butyraldehyde; production mix, at plant; 0.83 g/cm3, 130.23 g/mol | DE | agg | ts |
2-Ethylhexanol from propylene Aldolization of butyraldehyde; production mix, at plant; 0.83 g/cm3, 130.23 g/mol | EU-28 | agg | ts |
2K-dispersion adhesive mixing polyurethane, methyl ethyl ketone, water and hardener; production mix, at plant; contains 5% hardener | DE | agg | ts |
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 | ts |
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 | ts |
2-keto-L-gulonic acid preparation bacteria cultivation, fermentation of L- sorbose; production mix, at plant; 194.14 g/mol | US | agg | ts |
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 | ts |
3-Aminopropyltriethoxylsilane (estimation) reaction of chloroalkylsilane with ammonia or an organic amino compound; production mix, at plant; 0.946 g/cm3, 221.37 g/mol | DE | agg | ts |
3-Aminopropyltriethoxylsilane (estimation) 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 | ts |
3-Hydroxy-2-Naphthoic acid carboxylation of potassium naphtholate; production mix, at plant; 188.18 g/mol | DE | agg | ts |
3-Mercaptopropionic acid (estimation) 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 | ts |
4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (estimation) sulfonation of chlorobenzene; production mix, at plant; 287 g/mol | US | agg | ts |
4,4'-DCDPS (4,4'-Dichlorodiphenylsulfon) (estimation) sulfonation of chlorobenzene; production mix, at plant; 287 g/mol | DE | agg | ts |
4-Hydroxy 4-methyl-2-pentanone ketone condensation; single producer, at plant; density 0.931 g/mL at 25 °C, molar mass 116.16 g/mol | DE | agg | ts |
6-Hydroxy-2-Naphthoic acid carboxylation of potassium naphtholate; production mix, at plant; 188.18 g/mol | DE | agg | ts |
ABS GF 30 injection moulding of acrylonitrile butadiene styrene with glass fibres; production mix, at plant; 30% glass fibres | DE | agg | ts |
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 | DE | agg | ts |
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 | ts |
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 | ts |
Acetone Hock Process, oxidation of cumene; single route, at plant; 0.79 g/cm3, 58 g/mol | TH | agg | ts |
Acetone Hock Process, oxidation of cumene; single route, at plant; 0.79 g/cm3, 58 g/mol | JP | agg | ts |
Acetone Hock Process, oxidation of cumene; single route, at plant; 0.79 g/cm3, 58 g/mol | FR | agg | ts |
Acetone Hock Process, oxidation of cumene; single route, at plant; 0.79 g/cm3, 58 g/mol | CN | agg | ts |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product; production mix, at plant; 0.93 g/cm3, 85.11 g/mol | IT | agg | ts |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product; production mix, at plant; 0.93 g/cm3, 85.11 g/mol | DE | agg | ts |
Acetone cyanohydrin (ACH) with HCN from acrylonitrile by-product; production mix, at plant; 0.93 g/cm3, 85.11 g/mol | EU-28 | agg | ts |
Acetonitrile ammoxidation of propene; production mix, at plant; 786 mg/mL, 41 g/mol | GB | agg | ts |
Acetophenone (Phenyl methyl ketone) Friedel Crafts Alkylation of benzene; single route, at plant; 1.03 g/cm3, 120.15 g/mol | DE | agg | ts |
Acrylamide (catalytic hydrolysis) (50% solution) catalytic hydration of acrylonitrile; single producer, at plant; 1.13 g/cm3, 71.08 g/mol | DE | agg | ts |
Acrylamide (enzymatic hydration) (50% solution) enzymatic hydration of acrylonitrile; single producer, at plant; 1.13 g/cm3, 71.08 g/mol | DE | agg | ts |
Acrylate (emulsion) emulsion polymerization; single producer, at plant; 44% solid content | DE | agg | ts |
Acrylate (emulsion) emulsion polymerization; single route, at plant; 44% solid content | EU-28 | agg | ts |
Acrylate resin (epoxy functional) polymerisation; single route, at plant; 30.000- 100.000 g/mol | EU-28 | agg | ts |
Acrylate resin (epoxy-functional) polymerisation; single route, at plant; 30.000- 100.000 g/mol | DE | agg | ts |
Acrylate resin (solvent-systems) polymerisation; single route, at plant; 30.000- 100.000 g/mol | DE | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | NL | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | TH | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | BE | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | FR | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | CN | agg | ts |
Acrylic acid (Propene) oxidation of propene; production mix, at plant; 1.05 g/cm3, 72.06 g/mol | GB | agg | ts |
Acrylonitrile (AN) propene ammoxidation, by- product ammonium sulphate; production mix, at plant; 0.81 g/cm3, 53.06 g/mol | BE | agg | ts |
Acrylonitrile (AN) propene ammoxidation, by- product ammonium sulphate; production mix, at plant; 0.81 g/cm3, 53.06 g/mol | EU-28 | agg | ts |
Acrylonitrile-Butadiene-Styrene Granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene; production mix, at plant; 1.060- 1.080 g/cm3 | NL | agg | ts |
Acrylonitrile-Butadiene-Styrene Granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene; production mix, at plant; 1.060- 1.080 g/cm3 | BE | agg | ts |
Acrylonitrile-Butadiene-Styrene Granulate (ABS) polymerisation of acrylonitrile, butadiene and styrene; production mix, at plant; 1.060- 1.080 g/cm3 | DE | agg | ts |
Activated carbon technology mix; production mix, at plant; porous carbon structure | JP | agg | ts |
Activated carbon technology mix; production mix, at plant; porous carbon structure | EU-28 | agg | ts |
Activated carbon technology mix; production mix, at plant; porous carbon structure | CN | agg | ts |
Adhesive system MDF (35% H2O content) hydromethylation and condensation reactions of melamine, urea and formaldehyde; production mix, at plant; 35% H2O content | DE | agg | ts |
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 | ts |
Adhesive system mUF (36% moisture) hydromethylation and condensation reactions of urea and formaldehyde; production mix, at plant; 36% moisture | DE | agg | ts |
Adhesive system MUPF (35% H2O content) hydromethylation and condensation reactions of melamine, urea, phenol and formaldehyde; single route, at plant; 35% H2O | DE | agg | ts |
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 | ts |
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 | ts |
Adhesive system polyurethane-prepolymer reaction of methylene diisocyanate and polyether polyol; production mix, at plant; 50% methylene diisocyanate, 50% polyether polyol | DE | agg | ts |
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 | ts |
Adhesive system Urea Formaldehyde (UF) (35% H2O content) hydromethylation and condensation reactions of urea and formaldehyde; single producer, at plant; 35% H2O | DE | agg | ts |
Adipic acid oxidation of cyclohexane; production mix, at plant; 1.36 g/cm3, 146 g/mol | EU-28 | agg | ts |
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 | ts |
Air drying (food products) Air drying of food products using a Fluidized Bed Dryer; single operation, at producer; Fluidized Bed Dryer | US | p-agg | ts |
Air drying (food products) Air drying of food products using a Fluidized Bed Dryer; single operation, at producer; Fluidized Bed Dryer | EU-28 | p-agg | ts |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol; single route, at plant; estimation | US | agg | ts |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol; single route, at plant; estimation | DE | agg | ts |
Alcohol ethoxylate (ethoxylation) base- catalyzed ethoxylation of alcohol; single route, at plant; estimation | EU-28 | agg | ts |
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 | ts |
Aliphatic polyisocyanate prepolymer (IPDI-based) polyaddition of isophorone diisocyanate and polyol; production mix, at plant; 80% isocyanates, 20% polyols | DE | agg | ts |
Aliphatic polyisocyanate prepolymer (IPDI-based) polyaddition of isophorone diisocyanate and polyol; production mix, at plant; 80% isocyanates, 20% polyols | EU-28 | agg | ts |
Alkali resistent (AR) glass fibres from mineral components; single route, at plant; SiO2 63%, ZrO2 16,5%, Na2O 15 %, CaO 5,5% | DE | agg | ts |
Alkali-Xanthate reaction of sodium hydroxide with alcohol and carbon disulphide; production mix, at plant; 144 g/mol in when ethanol and sodium hydroxide are the educts | DE | agg | ts |
Alkyd resin (LM-system) condensation of polyols, polybasic acids or fatty acids; single route, at plant; LM-system | DE | agg | ts |
Alkyd resin (LM-system) condensation of polyols, polybasic acids or fatty acids; single producer, at plant; LM-system | EU-28 | agg | ts |
Allyl chloride (C3H5Cl) chlorination of propene; production mix, at plant; 0.94 g/cm3, 76.53 g/mol | BE | agg | ts |
Allyl chloride (C3H5Cl) chlorination of propene; production mix, at plant; 0.94 g/cm3, 76.53 g/mol | ES | agg | ts |
Allyl chloride (C3H5Cl) chlorination of propene; production mix, at plant; 0.94 g/cm3, 76.53 g/mol | NL | agg | ts |
AlNiCo magnet (estimation) metals casting; single route, at plant; 55% ferrite, 10% aluminium, 15% nickel, 20% cobalt | DE | agg | ts |
Alpha pinene (estimation) 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 | ts |
Aluminium (paste; H2O content) Hydropor atomizing AL powder, ball milling; single producer, at plant; particle size around 5- 35 microns | DE | agg | ts |
Aluminium chloride dissolving alumina in hydrochloric acid; single route, at plant; 2.44 g/cm3, 133.34 g/mol | DE | agg | ts |
Aluminium chloride (estimation) chlorination of alumium or alumina; single route, at plant; 2.44 g/cm3, 133.34 g/mol | EU-28 | agg | ts |
Aluminium chloride hexahydrate electrolytic reaction of aluminium and HCl; single route, at plant; 1.3 g/cm3, 241.43 g/mol | DE | agg | ts |
Aluminium diacetate (estimation) reaction of sodium aluminate and acetic acid; production mix, at plant; 162.1 g/mol | DE | agg | ts |
Aluminium extrusion profile (AlMg0.5Si) primary production; production mix, at plant; Alloy composition: 0.1%Cr, 0.1%Cu, 0.675%Mg, 0.1%Mn, 0.4%Si, 0.1%Ti, 0.1%Zn, 0.35%Fe | DE | agg | ts |
Aluminium extrusion profile (AlMg1SiCu) primary production; production mix, at plant; Alloy composition: 0.195%Cr, 0.275%Cu, 1%Mg, 0.15%Mn, 0.6%Si, 0.15%Ti, 0.25%Zn, 0.7%Fe | DE | agg | ts |
Aluminium extrusion profile (AlMgSi0,5) primary production; production mix, at plant; Alloy composition: 0,1%Cu, 0,45%Mg, 0,1%Mn, 0,45%Si, 0,1%Ti, 0,15%Zn, 0.2%Fe | DE | agg | ts |
Aluminium extrusion profile (AlZn5Mg1Zr) primary production; production mix, at plant; Alloy composition: 0.05%Cu, 1.05%Mg, 0.05%Mn, 0.1%Si, 0.05%Ti, 5%Zn, 0,185%Zr, 0.1%Fe | DE | agg | ts |
Aluminium flakes paste (chromated, 65% solids incl. solvents) wet milling process; single route, at plant; chromated, 65% solids | DE | agg | ts |
Aluminium flakes paste (chrome-free, 60% solids incl. solvents) wet milling process; single route, at plant; chrome-free, 60% solids | DE | agg | ts |
Aluminium fluoride reaction of bauxite, fluorspar and sulphuric acid; production mix, at plant; 2.88 g/cm3, 83.98 g/mol | EU-28 | agg | ts |
Aluminium foil technology mix of hot/ cold rolling and strip casting, cutting and packaging; production mix, at plant; 39% offcut, scrap recycling | DE | agg | ts |
Aluminium Hydroxide from Bauxite Bayer process; consumption mix, at plant; 2.42 g/cm3, 78.00 g/mol | EU-28 | agg | ts |
Aluminium ingot (AlMgSc) - Sc2O3 estimated with Ru - best case 0,02% Sc (estimation) primary production; production mix, at plant; Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.15%Ti, 0.02%Sc | DE | agg | ts |
Aluminium ingot (AlMgSc) - Sc2O3 estimated with Ru - worst case 0,4% Sc (estimation) primary production; production mix, at plant; Alloy composition: 0.2%Cu, 4.8%Mg, 0.3%Si, 0.15%Ti, 0.4%Sc | DE | agg | ts |
Aluminium ingot (AlMgSi0,5) primary production; production mix, at plant; Alloy composition:0.05%Cr, 0.1%Cu, 0.6%Mg, 0.1%Mn, 0.6%Si, 0.1%Ti, 0.15%Zn | DE | agg | ts |
Aluminium ingot (AlMgSi0,7) primary production; production mix, at plant; Alloy composition:0.6%Cr, 0.1%Cu, 0.9%Mg, 0.1%Mn, 0.6%Si, 0.1%Ti, 0.1%Zn | DE | agg | ts |
Aluminium ingot (AlMgSi1) primary production; production mix, at plant; Alloy composition:0.25%Cr, 0.1%Cu, 1.2%Mg, 1%Mn, 1.3%Si, 0.1%Ti, 0.2%Zn | DE | agg | ts |
Aluminium ingot (AlMn1Cu) primary production; production mix, at plant; Alloy composition:0.1%Cr, 0.1%Cu, 0.3%Mg, 1.5%Mn, 0.5%Si, 0.1%Ti, 0.2%Zn | DE | agg | ts |
Aluminium ingot (AlSi10MnMg) primary production; production mix, at plant; Alloy composition: 0.05%Cu, 0.35%Mg, 0.35%Mn, 10.25%Si, 0.2%Ti, 0.07%Zn, 0.25%Fe | DE | agg | ts |
Aluminium ingot (AlSi7Mg0,3) primary production; production mix, at plant | DE | agg | ts |
Aluminium nitrate (estimation) reaction of aluminium hydroxide with nitric acid; single route, at plant; 1.72 g/cm3, 213 g/mol | EU-28 | agg | ts |
Aluminium oxide (Al2O3 high purity) Bayer process; production mix, at plant; 3.94 g/cm3, 101.96 g/mol | DE | agg | ts |
Aluminium sheet (AlMg4.5Mn0.4) primary production; production mix, at plant; Alloy composition: Cr 0,1%; Cu 0,15%; Mg 4,5 %; Mn 0,35%; Si 0,2%; Ti 0,1%; Zn 0,25%; Fe 0,35% | DE | agg | ts |
Aluminium sheet (AlSi1.2Mg0.4) primary production; production mix, at plant; Alloy composition: Cr 0,1%; Cu 0,2%; Mg 0,775 %; Mn 0,2%; Si 1,25%; Ti 0,15%; Zn 0,2%; Fe 0,5% | DE | agg | ts |
Aluminium sheet (AlZn5.5Mg1.5) primary production; production mix, at plant; Alloy composition: Cr 0,05%; Cu 0,25%; Mg 1,5 %; Mn 0,1%; Si 0,25%; Ti 0,1%; Zn 5,5%; Zr 0,13 %; Fe 0,4% | DE | agg | ts |
Aluminium sheet (AlZn5.5MgCu) primary production; production mix, at plant; Alloy composition: Cr 0,23%; Cu 1,6%; Mg 2,5 %; Mn 0,3%; Si 0,4%; Ti 0,2%; Zn 5,6%; Zr 0 %; Fe 0,5% | DE | agg | ts |
Aluminium silicate (zeolite type A) from aluminum, silica, desired ions, and sodium hydroxide; production mix, at plant; 162.05 g/mol | DE | agg | ts |
Aluminium sulphate (estimation) from aluminium hydroxide and sulphuric acid; single route, at plant; 2.71 g/cm3, 342.15 g/mol | DE | agg | ts |
Aluminium sulphate (estimation) via aluminium hydroxide and sulphuric acid; single route, at plant; 2.71 g/cm3, 342.15 g/mol | EU-28 | agg | ts |
Aluminium sulphate (estimation) via aluminium hydroxide and sulphuric acid; single route, at plant; 2.71 g/cm3, 342.15 g/mol | US | agg | ts |
Aluminium sulphate from aluminium pig (estimation) via aluminium ingot and sulphuric acid; single route, at plant; 2.71 g/cm3, 342.15 g/mol | DE | agg | ts |
Aluminium Trilactate/Aluminium Lactate reaction of lactic acid with aluminium hydroxide; production mix, at plant; 294.19 g/mol | DE | p-agg | ts |
Amine adduct emulsion on an aqueous base (estimation) polymerisation of a bisphenol A resin with a polyamine; single route, at plant; 55% polymer, 45% water | EU-28 | agg | ts |
Amine adduct emulsion on an aqueous base (estimation) polymerisation of a bisphenol A resin with a polyamine; single route, at plant; 55% polymer, 45% water | DE | agg | ts |
Amino trimethylene phosphonic acid, sodium salt (estimation) reaction of ammonium chloride, formaldehyde and phosphoric acid; production mix, at plant; 1.33 g/cm3, 299.05 g/mol | EU-28 | agg | ts |
Amino trimethylene phosphonic acid, sodium salt (estimation) reaction of ammonium chloride, formaldehyde and phosphoric acid; production mix, at plant; 1.33 g/cm3, 299.05 g/mol | DE | agg | ts |
Ammonia (high purity) purified with activated carbon; single route, at plant; 0.7714 kg/m3, 17.03 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (economic allocation) Haber-Bosch process, from coal; single, at plant; 0.7714 kg/m3, 17.03 g/mol | CN | agg | ts |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide, feedstock coal (without allocation) Haber-Bosch process, from coal; single, at plant; 0.7714 kg/m3, 17.03 g/mol | CN | p-agg | ts |
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 | ts |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air) Haber-Bosch process, from natural gas; single route, at plant; 0.7714 kg/m3, 17.03 g/mol | BR | agg | ts |
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 | ts |
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 | ts |
Ammonia (NH3) without CO2 recovery, feedstock coal (carbon dioxide emissions to air) Haber-Bosch process, from coal; single, at plant; 0.7714 kg/m3, 17.03 g/mol | CN | agg | ts |
Ammonia solution, NH3 (aq.) (estimation) Haber-Bosch process, from natural gas, diluted solution; production mix, at plant; 35% concentrated | EU-28 | agg | ts |
Ammonia water (weight share 25% NH3) ammonium mixed with water; production mix, at plant; weight share 25% NH3 | DE | agg | ts |
Ammonium chloride (salmiac, Solvay-process) Solvay process; single route, at plant; 1.53 g/cm3, 53.49 g/mol | EU-28 | agg | ts |
Ammonium hydrogen carbonate reacting ammonia with CO2; single route, at plant; 1.59 g/cm3, 79.06 g/mol | DE | agg | ts |
Ammonium hydrogen carbonate (Ammonium bicarbonate) reacting ammonia with CO2; single producer, at plant; 1.59 g/cm3, 79.06 g/mol | EU-28 | agg | ts |
Ammonium nitrate (ON, BAT, 68% solution) from nitric acid; production mix, at plant; 1.73 g/cm3, 80.04 g/mol | AU | agg | ts |
Ammonium sulphate (co product Acetone cyanohydrin) with hydrogen cyanide from acrylonitrile by-product; single route, at plant; 1.77 g/cm3, 132.14 g/mol | EU-28 | agg | ts |
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 | ts |
Ammonium sulphate by-product caprolactam from phenol from phenol; single route, at plant; 1.77 g/cm3, 132.14 g/mol | NL | agg | ts |
Ammonium sulphate mix (by-product), 50:50 technology mix; production mix, at plant; 1.77 g/cm3, 132.14 g/mol | EU-28 | agg | ts |
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 | ts |
Ammoniumpolyphosphate from urea and phoshoric acid; production mix, at plant; 1,9 g/cm3, 97.01 g/mol | DE | agg | ts |
Anhydrite (CaSO4) (natural) technology mix (mining and open pit mining); production mix, at producer; 2.96 g/cm3 | DE | agg | ts |
Anhydrite (CaSO4) (natural) (EN15804 A1-A3) technology mix (mining and open pit mining); production mix, at producer; 2.96 g/cm3 | EU-28 | agg | ts |
Anhydrite (CaSO4) (thermal) (EN15804 A1-A3) thermal produced anhydrite; production mix, at plant; grinded and purified product | EU-28 | agg | ts |
Aniline (Phenyl amine, Amino benzene) catalytic hydrogenation of nitrobenzene; single route, at plant; 1.022 g/cm3, 93.13 g/mol | BR | agg | ts |
Aniline (Phenyl amine, Amino benzene) catalytic hydrogenation of nitrobenzene; single route, at plant; 1.022 g/cm3, 93.13 g/mol | EU-28 | agg | ts |
Anthraquinone via reformate from pyrolysis gas; single route, at plant; 1.31 g/cm3, 208.22 g/mol | DE | agg | ts |
Anthraquinone via naphthalene via naphthalene; single route, at plant; 1.31 g/cm3, 208.22 g/mol | DE | agg | ts |
Antimony trioxide primary production, antimony ore mining, roasting; single route, at plant; 5.2 g/cm3, 291.5 g/mol | EU-28 | agg | ts |
Application primer (waterproof) water proof application; single route, at plant; application per m2 | US | agg | ts |
Application primer (waterproof) water proof application; single route, at plant; application per m2 | EU-28 | agg | ts |
Aramide fiber (para aramid) condensation of para- phenylene diamine and terephthaloyl dichloride; single route, at plant; para aramid | DE | agg | ts |
Argon (gaseous) cryogenic air fractionation; production mix, at plant; 40 g/mol | CN | agg | ts |
Aromatics (BTX) at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Aromatics (BTX) at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Aromatics (BTX) at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Ascorbic acid Reichstein Synthesis, from glucose; single route, at plant; 1.65 g/cm3, 176.12 g/mol | DE | agg | ts |
Asphalt binder (rolling asphalt) combination of aggregates and bitumen; production mix, at plant; 170 - 250 kg/m2 | DE | agg | ts |
Average load of laundry average washing machine, for domestic textile cleaning; production mix, at plant; energy consumption 2.25 kWh/ load, water consumption 23 gal/load | US | p-agg | ts |
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 | ts |
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 | ts |
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 | ts |
Azodicarbonamide (propellant) from hydrazine and urea; single route, at plant; 1.65 g/cm3, 116.08 g/mol | DE | agg | ts |
Bamboo cultivation (80% H2O content) technology mix; production mix, at producer; 80% H2O | CN | agg | ts |
Barge, 1,500t payload capacity / canal technology mix, diesel driven, cargo; consumption mix; 1,500t payload capacity/ canal | GLO | u-so | ts |
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 | ts |
Barium chloride (estimation) reaction of barium sulphide and hydrochloric acid; production mix, at plant; 3.86 g/cm3, 208.23 g/mol | DE | agg | ts |
Barium hydroxide (estimation) reaction of barium sulphide and sodium hydroxide; single route, at plant; 3.74 g/cm3, 171.34 g/mol | EU-28 | agg | ts |
Barium magnesium aluminate (BAM) from Al2O3, BaCO3, MgCO3, and Eu2O3; single route, at plant; 1202 g/mol | GLO | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Barium sulphide (100%) carbothermal reduction of barium sulphate; production mix, at plant; 4.25 g/cm3, 169.39 g/mol | DE | agg | ts |
Barium zinc stearate (stabiliser, estimation) production of barium stearate and zinc stearate, mixing; production mix, at plant; 60% barium stearate, 40% zinc stearate | EU-28 | agg | ts |
Basalt production (washed) basalt mining and crushing; single producer, at plant; <52% SiO2 | EU-28 | agg | ts |
Basalt production (washed) basalt mining and crushing; single producer, at plant; <52% SiO2 | DE | agg | ts |
Base oil (group I) (solvent refined) from crude oil; production mix, at refinery; 40 MJ/kg net calorific value | EU-28 | agg | ts |
Base oil (group II) (hydrotreated) from crude oil; production mix, at refinery; 40 MJ/kg net calorific value | EU-28 | agg | ts |
Base oil (group III) (hydrocracked) from crude oil; production mix, at refinery; 40 MJ/kg net calorific value | EU-28 | agg | ts |
Beech log free forest track forest cultivation, harvesting, wet storage; production mix, at plant; 660 kg/m3 | DE | agg | ts |
Beech log free forest track forest cultivation, harvesting, wet storage; production mix, at plant; 660 kg/m3 | EU-28 | agg | ts |
Beech log free forest track (20 % H2O content) forest cultivation, harvesting, wet storage; production mix, at plant; 25% moisture, 20% H2O content included in wood | EU-28 | agg | ts |
Beef filet (cattle slaughterhouse) (economic allocation) slaughterhouse; single producer, at plant; boneless beef filet | DE | agg | ts |
Bentonite, natural mining and beneficiation; production mix, at plant; composed primarily of smectite minerals | CN | agg | ts |
Bentonite, natural mining and beneficiation; production mix, at plant; composed primarily of smectite minerals | RU | agg | ts |
Bentonite, natural mining and beneficiation; production mix, at plant; composed primarily of smectite minerals | IN | agg | ts |
Bentonite, natural mining and beneficiation; production mix, at plant; composed primarily of smectite minerals | EU-28 | agg | ts |
Bentonite, natural mining and beneficiation; production mix, at plant; composed primarily of smectite minerals | DE | agg | ts |
Benzanthrone from sulphuric acid and anthrone; single route, at plant; 230.27 g/mol | US | agg | ts |
Benzene from pyrolysis fuel; production mix, at plant; 0.88 g/cm3, 78 g/mol | ES | agg | ts |
Benzene dealkylation of toluene; production mix, at plant; 0.88 g/cm3, 78 g/mol | GB | agg | ts |
Benzene dealkylation of toluene; production mix, at plant; 0.88 g/cm3, 78 g/mol | IT | agg | ts |
Benzene dealkylation of toluene; production mix, at plant; 0.88 g/cm3, 78 g/mol | FR | agg | ts |
Benzene dealkylation of toluene; production mix, at plant; 0.88 g/cm3, 78 g/mol | NL | agg | ts |
Benzene (from reformate) from reformate; production mix, at plant; 0.88 g/cm3, 78 g/mol | GB | agg | ts |
Benzene (from reformate) from reformate; production mix, at plant; 0.88 g/cm3, 78 g/mol | FR | agg | ts |
Benzene (from reformate) from reformate; production mix, at plant; 0.88 g/cm3, 78 g/mol | IT | agg | ts |
Benzene (from reformate) (estimation) from reformate; production mix, at plant; 0.88 g/cm3, 78 g/mol | TH | agg | ts |
Benzene (from reformate) (estimation) from reformate; production mix, at plant; 0.88 g/cm3, 78 g/mol | CN | agg | ts |
Benzene by-product ethine (acetylene) Sachsse Bartholome Process; single route, at plant; 0.88 g/cm3, 78 g/mol | DE | agg | ts |
Benzene mix technology mix; production mix, to consumer | US | agg | ts |
Benzene mix technology mix; production mix, at plant; 0.88 g/cm3, 78 g/mol | GB | agg | ts |
Benzene sulfonic acid sulfonation of benzene; single route, at plant; 1.32 g/cm3 (47 °C), 158.18 g/mol | DE | agg | ts |
Benzene sulfonic acid (estimate) sulfonation of benzene; single producer, at plant; 1.32 g/cm3 (47 °C), 158.18 g/mol | US | agg | ts |
Benzene sulfonic acid (estimate) sulfonation of benzene; single producer, at plant; 1.32 g/cm3 (47 °C), 158.18 g/mol | EU-28 | agg | ts |
Benzoic acid ester esterification of hydroxybenzoic acid with ethanol; production mix, at plant; 166 g/mol | EU-28 | agg | ts |
Benzotrichloride (estimation) chlorination of toluene; production mix, at plant; 1.38 g/cm3, 195.48 g/mol | US | agg | ts |
Benzoyl Chloride (estimation) reaction of benzoyl trichloride with water; single route, at plant; 1.21 g/cm3, 140.57 g/mol | US | agg | ts |
Benzoyl Peroxide production from benzoyl chloride and hydrogen peroxide; production mix, at plant; 1.33 g/cm3, 242.23 g/mol | US | agg | ts |
Benzyl alcohol hydrolysis of benzyl chloride; single route, at plant; 1.04 g/cm3, 108.14 g/mol | EU-28 | agg | ts |
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), at plant; 34.6 MJ/kg net calorific value | EU-28 | p-agg | ts |
Beta pinene (estimation) 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 | ts |
BF slag incl. grinding BF route; production mix and grinding, at plant; assemblage of Ca-Al-Mg silicates | AE | agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 %; Al 0,015 % | DE | p-agg | ts |
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 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,003 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,02 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,25%; B 0,005% | DE | p-agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 %; Al 0,015 % | DE | p-agg | ts |
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 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,003 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,02 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,045 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 %; Al 0,015 % | DE | p-agg | ts |
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 %; Al 0,01 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,003 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,025 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,015 %; Cr+Mo 0,6%; Ti+Nb 0,2%; B 0,005% | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,02 %; Al 0,01 %; 0,3%Ti | DE | p-agg | ts |
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 0,025 %; Al 0,015 %, Nb 0,09 % | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1,4%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005 | DE | p-agg | ts |
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 0,01 %; Cr+Mo 1%; Ti+Nb 0,15%; B 0,005% | DE | p-agg | ts |
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 0,015 %; Cr+Mo 1%; Ti+Nb 0,25%; B 0,005 | DE | p-agg | ts |
Biaxial oriented PA film (BOPA PA6) polyamide 6 extrusion and stretching; single route, at plant; 32 MJ/kg net calorific value | DE | agg | ts |
Biaxial oriented PET film (BOPET) PET extrusion and stretching; single route, at plant; 192.17 g/mol per repeating unit | DE | agg | ts |
Biaxial oriented polypropylene film (BOPP) polypropylene extrusion and stretching; single producer, at plant; 44 MJ/kg net calorific value | DE | agg | ts |
Biaxial oriented polypropylene film (BOPP) polypropylene extrusion and stretching; single producer, at plant; 44 MJ/kg net calorific value | US | agg | ts |
Biaxial oriented Polystyrene film (BOPS) polystyrene extrusion and stretching; single route, at plant; 40 MJ/kg net calorific value | DE | agg | ts |
Bicomponent fiber (PET/PA) spinning of polyethylene terephthalate, polyamide and epoxy resin; production mix, at plant; 85% PET, 15% PA | DE | agg | ts |
Biodiesel based on rape seed methyl ester (RME) from rape seeds; production mix, at plant; 78% total carbon content, 74% biogenic carbon content, 37 MJ/kg net calorific value | EU-28 | agg | ts |
Bioethanol (from corn) from corn; production mix, at plant; 55% carbon content, 26.8 MJ net calorific value | EU-28 | agg | ts |
Bioethanol from corn, at plant from corn; production mix, at plant; 55% carbon content, 26.8 MJ net calorific value | US | agg | ts |
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 | ts |
Bioethanol from sugar beet, at plant from sugar beet; single route, at plant; 0.79 g/cm3, 46.07 g/mol | DE | agg | ts |
Bioethanol from sugar cane (no slash and burn) (estimation) from sugar cane; single route, at plant; 0.79 g/cm3, 46.07 g/mol | BR | agg | ts |
Bioethanol from sugar cane, at plant from sugar cane; production mix, at plant; 52% carbon content, 26.8 MJ net calorific value | BR | agg | ts |
Bioethanol from wheat (DDGS internal energy) from wheat; single route, at plant; 0.79 g/cm3, 46.07 g/mol | EU-28 | agg | ts |
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 | ts |
Bioethanol from wheat, at plant transport, conditioning and fermentation of wheat; single route, at plant; 55% carbon content, 26.8 MJ net calorific value | US | agg | ts |
Biogas for bioenergy technology mix; consumption mix, to consumer | GB | agg | ts |
Biogas for bioenergy technology mix; consumption mix, to consumer | DE | agg | ts |
Biogas for bioenergy technology mix; consumption mix, to consumer | NL | agg | ts |
Biogas from cattle liquid manure 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 value | DE | p-agg | ts |
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 value | DE | p-agg | ts |
Biogas from cattle solid manure 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 value | DE | p-agg | ts |
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 value | DE | p-agg | ts |
Biogas from kitchen residues 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 value | DE | p-agg | ts |
Biogas from Maize for bioenergy technology mix / Anaerobic fermentation of maize silage from whole plants to biogas via wet fermentation prosess; production mix, at producer, gate to gate; Biogas net calorific value is 15MJ/kg (~30% (mass) methane content) | DE | p-agg | ts |
Biogas from municipal organic waste 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 value | DE | p-agg | ts |
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 value | DE | p-agg | ts |
Biogas from pig liquid manure 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 value | DE | p-agg | ts |
Biogas from poultry solid manure 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 value | DE | p-agg | ts |
Biogas from sugar beet leaves 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 value | DE | p-agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | BR | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | NL | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | GB | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | CA | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | HU | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | DK | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | US | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | PT | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | TH | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | FI | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | DE | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | SE | agg | ts |
Biomass (solid) for bioenergy technology mix; consumption mix, to consumer | NZ | agg | ts |
Biomass Power Plant - CHP (lumber, 12% moisture) cogeneration electricity and heat, technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | p-agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Bisphenol A technology mix; production mix, at plant; solid, density: 1,2 g·cm−3, molar mass: 228,28 g·mol−1 | EU-28 | agg | ts |
Bitumen at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Bitumen at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Bitumen at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Blast Furnace slag iron production, blast furnace route, by- product slag, grinded; single route, at plant; 2800- 4000 kg/m³ | IN | agg | ts |
Blood from pig, unprocessed, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Blood meal from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Blood meal from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Blood meal from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Blood meal from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Blood meal from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Blood meal from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Blood meal from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Blood meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Blood meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Blood meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Blood meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | ZA | agg | ts |
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 | ts |
Boiler ash from hard coal power plant from hard coal power plant; production mix, at power plant; grain size ca. 13 mm | DE | agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | p-agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | p-agg | ts |
Boneless pork, from pig slaughterhouse (economic allocation) - open input pig raising slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | p-agg | ts |
Boneless pork, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Borax (dehydrated) via dehydration; production mix, at plant; 201.37 g/mol | DE | agg | ts |
Borax (dehydrated) via dehydration; production mix, at plant; 201.37 g/mol | EU-28 | agg | ts |
Borax pentahydrate via colemanite; production mix, at plant; 291 g/mol | DE | agg | ts |
Borax pentahydrate via colemanite; production mix, at plant; 291 g/mol | EU-28 | agg | ts |
Boric acid (estimation) reaction of borax pentahydrate and sulfuric acid; single route, at plant; 1.44 g/cm3, 61.83 g/mol | EU-28 | agg | ts |
Boric acid (estimation) reaction of borax pentahydrate and sulfuric acid; single route, at plant; 1.44 g/cm3, 61.83 g/mol | DE | agg | ts |
Boric acid by-product sodium sulfate (estimation) reaction of borax pentahydrate and sulfuric acid; single route, at plant; 1.44 g/cm3, 61.83 g/mol | US | agg | ts |
Brass die-casting (CuZn20) die casting, from copper and zinc, primary production; single route, at plant; 80% copper, 20% zinc | DE | p-agg | ts |
Bromine (from sea water) estimation from sea water; single route, at plant; 3.10 g/cm3, 79.90 g/cm3 | GB | agg | ts |
Bunker oil at refinery from crude oil; production mix, at refinery; 3.5 wt.% sulphur | MY | agg | ts |
Bunker oil at refinery from crude oil; production mix, at refinery; 3.5 wt.% sulphur | RU | agg | ts |
Bunker oil at refinery from crude oil; production mix, at refinery; 3.5 wt.% sulphur | NL | agg | ts |
Butane at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Butane at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Butane at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Butane diamine ( Tetramethylenediamine TMDA) (estimation) reaction of acrylonitrile, hydrogen cyanide and hydrogen; single route, at plant; 0.88 g/cm3, 88.15 g/mol | CN | agg | ts |
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 | ts |
Butanediol from propylene oxide (PO chlorohydrine) from propylene oxide; single route, at plant; 1.02 g/cm3, 90.12 g/mol | US | agg | ts |
Butanediol from propylene oxide (PO oxirane) from propylene oxide; single route, at plant; 1.02 g/cm3, 90.12 g/mol | US | agg | ts |
Butanol (n-butanol) from propylene Oxo synthesis, from propylene with rhodium catalyst; production mix, at producer; 0.81 g/cm3, 74.12 g/mol | EU-28 | agg | ts |
Butanol (n-butanol) from propylene Oxo synthesis, from propylene with rhodium catalyst; production mix, at producer; 0.81 g/cm3, 74.12 g/mol | DE | agg | ts |
Butyl Acetate Fischer esterification; production mix, at plant; 0.88 g/cm3, 116.16 g/mol | US | agg | ts |
Butyl acetate Fischer esterification; production mix, at plant; 0.88 g/cm3, 116.16 g/mol | EU-28 | agg | ts |
Butyl acetate Fischer esterification; production mix, at plant; 0.88 g/cm3, 116.16 g/mol | DE | agg | ts |
Butyl acrylate esterification of acrylic acid and butanol; single producer, at plant; density 0,90 g·cm−3, molar mass 128,17 g·mol−1 | EU-28 | agg | ts |
Butyl acrylate esterification of acrylic acid and butanol; single producer, at plant; density 0,90 g·cm−3, molar mass 128,17 g·mol−1 | DE | agg | ts |
Butyldiglycol ethoxylation of butanol; production mix, at plant; liquid, density: 0,95 g·cm−3, molar mass: 162,23 g·mol−1 | DE | agg | ts |
Butyldiglycol acetate (estimation) from butyldiglycol and butyl acetate; single route, at plant; 0.98 gcm-3 at 20°C, 104.27 g/mol | DE | agg | ts |
Butylene at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Butylene at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Butylene at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Butyraldehyde Oxo process, by-product butanol from propylene with rhodium catalyst; production mix, at plant; 0.80 g/cm3, 72.11 g/mol | DE | agg | ts |
Butyraldehyde Oxo process, by-product butanol from propylene with rhodium catalyst; production mix, at plant; 0.80 g/cm3, 72.11 g/mol | EU-28 | agg | ts |
Butyraldehyde by-product butanol from propylene Oxo process, by-product butanol from propylene with rhodium catalyst; production mix, at plant; 0.80 g/cm3, 72.11 g/mol | CN | agg | ts |
Butyraldehyde by-product butanol from propylene Oxo process, by-product butanol from propylene with rhodium catalyst; production mix, at plant; 0.80 g/cm3, 72.11 g/mol | US | agg | ts |
Butyric acid anhydride liquid- phase oxidation of butyraldehyde; single route, at plant; 0.967 g/cm3, molar mass 158.19 g/mol | DE | agg | ts |
C10-Methylester including transesterification and fractionation Crude coconut oil processing, transesterification and fractionation; single producer, at plant; C10 methyl ester fraction | MY | agg | ts |
C12-Methylester including transesterification and fractionation Palm kernel oil processing, transesterification and fractionation; single producer, at plant; C12 methyl ester fraction | MY | agg | ts |
C4 cut (butadiene) steam cracker; production mix, at plant; 45.3 MJ net calorific value | FR | agg | ts |
C4 cut (butadiene) (estimation) steam cracker; production mix, at plant; 45.3 MJ net calorific value | JP | agg | ts |
C4 cut (butadiene) (estimation) steam cracker; production mix, at plant; 45.3 MJ net calorific value | ES | agg | ts |
C4 cut (butadiene) (estimation) steam cracker; production mix, at plant; 45.3 MJ net calorific value | CN | agg | ts |
C4 cut from FCC at refinery from crude oil; production mix, at refinery | DE | agg | ts |
C-6 fluorinated acrylic copolymer Esterification of 2-(Perfluorohexyl)ethanol by acrylic acid; single route, at producer; MW=418.15 g/mol | US | agg | ts |
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 | ts |
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 | ts |
Cable 1-core power 18AWG mPPE (10 g/m) D1.7 technology mix; production mix, at plant; tinned Cu wire, mPPE insulation | GLO | agg | ts |
Cable 1-core power 18AWG PE (16 g/m) D2.8 technology mix; production mix, at plant; tinned Cu wire, PE insulation | GLO | agg | ts |
Cable 1-core power 18AWG PTFE (13 g/m) D1.7 technology mix; production mix, at plant; tinned Cu wire, PTFE insulation | GLO | agg | ts |
Cable Ethernet Cat-6 PE/PVC (66 g/m) D6.4 technology mix; production mix, at plant; bare Cu wire, PE insulation, PVC jacket, unshielded | GLO | agg | ts |
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, shielded | GLO | agg | ts |
Cadmium acetate (estimation) reaction of cadmium oxide with acetic acid; single route, at plant; 2.34 g/cm3, 230.50 g/mol | US | agg | ts |
Calcined kaolin powder (Al2O3 * SiO2) calcination in rotary furnace; single route, at plant; 162.06 g/mol | DE | agg | ts |
Calcined petroleum coke calcination; single route, at plant; 95 to 99 wt% carbon content | CN | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Calcium diformate reaction of finelime and formaldehyde; single route, at plant; stoichiometrical estimation, density 2,02 g·cm−3, molar mass 130,11 g·mol−1 | DE | agg | ts |
Calcium diformate (estimation) reaction of finelime and formaldehyde; single route, at plant; stoichiometrical estimation, density 2,02 g·cm−3, molar mass 130,11 g·mol−1 | EU-28 | agg | ts |
Calcium sulfoaluminate cement from alumina, gypsum and limestone via furnace process; single route, at producer; CSA cement requires kiln temperatures of around 1250°C (2250°F) | US | agg | ts |
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 | ts |
Carbon dioxide by-product ethylene oxide (EO) from air oxidation of ethylene with air; single route, at plant; 1.98 kg/m3, 44.01 g/mol | GB | agg | ts |
Carbon dioxide by-product ethylene oxide (EO) from air oxidation of ethylene with air; single route, at plant; 1.98 kg/m3, 44.01 g/mol | BE | agg | ts |
Carbon dioxide by-product ethylene oxide (EO) from air oxidation of ethylene with air; single route, at plant; 1.98 kg/m3, 44.01 g/mol | FR | agg | ts |
Carbon dioxide by-product ethylene oxide (EO) from air oxidation of ethylene with air; single route, at plant; 1.98 kg/m3, 44.01 g/mol | NL | agg | ts |
Carbon dioxide by-product ethylene oxide (EO) from air oxidation of ethylene with air; single route, at plant; 1.98 kg/m3, 44.01 g/mol | DE | agg | ts |
Carbon dioxide by-product ethylene oxide (EO) via O2/methane oxidation of ethylene with oxygen; single route, at plant; 1.98 kg/m3, 44.01 g/mol | DE | agg | ts |
Carbon dioxide highly pure dewatering, trace removal; single route, at plant; 1,98 kg/m3, 44 g/mol | DE | agg | ts |
Carbon fiber yarn (CF; from PAN; intermediate strength) spinning, stabilizing, carbonizing, surface treatment, sizing; single producer, at plant; from PAN, intermediate strengths 42 million psi tensile modulus (estimation) | DE | agg | ts |
Carbon monoxide (via synthesis gas) 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 | ts |
Cargo hauled by freight diesel train (indirect) diesel driven, cargo; consumption mix; average train, gross tonne weight 1000t, 726t payload capacity | EU-28 | agg | ts |
Cargo hauled by freight electric train (indirect) electricity driven, cargo; consumption mix; average train, gross tonne weight 1000t, 726t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck trailer, 22 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck trailer, 22 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck trailer, 22 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 11.4 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 11.4 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 11.4 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 17.3 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 17.3 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 17.3 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 22 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 22 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 22 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 24.7 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 24.7 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 24.7 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 3.3 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 3.3 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 3.3 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 5 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 5 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 5 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 9.3 t payload [tkm] diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 9.3 t payload [tkm] (direct) diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Cargo hauled by truck, 9.3 t payload [tkm] (indirect) diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Casein glue (PVAC dispersion) polymerization of vinyl acetate, PVAC dispersion in water; single route, at plant; 50% FKA | DE | agg | ts |
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; 76,5 wt.% biogenic carbon content | IN | agg | ts |
Cassava dry chips (mechanical chopping and sun drying) mechanical chopping and sun-drying; single route, at producer; 10% H2O | TH | agg | ts |
Castor oil (average) castor oil pressing; single route, at plant; 72,5% carbon content | IN | agg | ts |
Cattle hide, fresh, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Cattle hide, fresh, from slaughterhouse (economic allocation) - open input cattle raising slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | p-agg | ts |
Cattle hide, fresh, from slaughterhouse (economic allocation) - open input cattle raising slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | DE | p-agg | ts |
Cellulose based on timber spruce; production mix, at plant; 1.5 g/cm3 | US | agg | ts |
Cellulose (estimation, based on US foreground system) based on timber spruce; production mix, at plant; estimation | DE | agg | ts |
Cellulose acetate butyrate (estimation) viscose process; single producer, at plant; estimation | DE | agg | ts |
Cement (CEM III/B) Blastfurnance Cement technology mix; production mix, at plant; CEM III B, 25% clinker, 75% BF slag | DE | agg | ts |
Cement (CEM III/C) Blastfurnance Cement technology mix; production mix, at plant; CEM III C, 10% clinker, 90% BF slag | DE | agg | ts |
Cement average grinding - open input cement clinker materials grinding at grinding plant; single route at plant; 3000 kg/m3 | DE | p-agg | ts |
Ceramic (Passive components) including slurry preparation, shaping and burning; single route, at plant; Al2O3, silica sand, MnO2 mixture | GLO | agg | ts |
Cerium oxide mix Rare earth element mining and processing; single producer, at plant; 85% China (Inner Mongolia Bayun Obo), 15% USA (Mountain Pass, California), monazite and bastnaesite ores | GLO | agg | ts |
Chlorinated Paraffins (estimation) reaction of paraffins with chlorine; production mix, at plant; 1.10- 1.26 g/cm3 | DE | agg | ts |
Chlorinated Polyethylene (estimation) reaction of polyethylene with chlorine; production mix, at plant; 1.27- 1.37 g/cm3 | DE | agg | ts |
Chlorine acetic acid (estimation) chlorination of acetic acid; single route, at plant; 1.58 g/cm3, 94.50 g·mol−1 | US | agg | ts |
Chlorine dioxide (1% ClO, 99% H2O; chlorate based process; SVP-LITE) (estimation) reduction of sodium chlorate with methanol; single route, at plant; 2.76 kg/m3, 67.45 g/mol | EU-28 | agg | ts |
Chlorine from chlorine-alkali-electrolysis (amalgam) chlorine alkali electrolysis, amalgam; single route, at plant; 3.2 g/l, 70.9 g/mol | IN | agg | ts |
Chlorine from chlorine-alkali-electrolysis (amalgam) chlorine alkali electrolysis, amalgam; single route, at plant; 3.2 g/l, 70.9 g/mol | EU-28 | agg | ts |
Chlorine from chlorine-alkali-electrolysis (amalgam) chlorine alkali electrolysis, amalgam; single route, at plant; 3.2 g/l, 70.9 g/mol | BE | agg | ts |
Chlorine from chlorine-alkali-electrolysis (amalgam) chlorine alkali electrolysis, amalgam; single route, at plant; 3.2 g/l, 70.9 g/mol | ES | agg | ts |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm; single route, at plant; 3.2 g/l, 70.9 g/mol | AU | agg | ts |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm; single route, at plant; 3.2 g/l, 70.9 g/mol | NO | agg | ts |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm; single route, at plant; 3.2 g/l, 70.9 g/mol | EU-28 | agg | ts |
Chlorine from chlorine-alkali-electrolysis (diaphragm) chlorine alkali electrolysis, diaphragm; single route, at plant; 3.2 g/l, 70.9 g/mol | CN | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | ES | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | AU | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | IN | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | JP | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | PT | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | NL | agg | ts |
Chlorine from chlorine-alkali-electrolysis (membrane) chlorine alkali electrolysis, membrane; single route, at plant; 3.2 g/l, 70.9 g/mol | NO | agg | ts |
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 | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | AU | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | JP | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | PL | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | SE | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | PT | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | EU-28 | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | CZ | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 g/l, 70.9 g/mol | IN | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | HU | agg | ts |
Chlorine mix technology mix; production mix, at plant; 3.2 kg/m3, 70.9 g/mol | RO | agg | ts |
Chloroacetic acid (estimation) chlorination of acetic acid; single route, at plant; 1.58 g/cm3, 94.50 g·mol−1 | DE | agg | ts |
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 | ts |
Chloroacetylic acid from acetic acid chlorination of acetic acid; single route, at plant; 1.58 g/cm3, 94.50 g·mol−1 | DE | agg | ts |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene; production mix, at plant; 1.11 g/cm3, 112.56 g/mol | DE | agg | ts |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene; production mix, at plant; 1.11 g/cm3, 112.56 g/mol | EU-28 | agg | ts |
Chlorobenzene (by product chlorobenzene, hydrochloric acid) chlorination of benzene; production mix, at plant; 1.11 g/cm3, 112.56 g/mol | JP | agg | ts |
Chlorobenzotrifluoride (p-) from chlorotoluene, chlorine and hydrogen fluoride; production mix, at plant; 180.55 g/mol | DE | agg | ts |
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 | ts |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride; production mix, at plant; 3.94 kg/m3, 86.47 g/mol | GB | agg | ts |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride; production mix, at plant; 3.94 kg/m3, 86.47 g/mol | DE | agg | ts |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride; production mix, at plant; 3.94 kg/m3, 86.47 g/mol | NL | agg | ts |
Chlorodifluoromethane (R22, HCFC-22) reaction of trichloromethane with hydrogen fluoride; production mix, at plant; 3.94 kg/m3, 86.47 g/mol | IT | agg | ts |
Chlorodifluoromethane (R22, HCFC-22) (estimation) reaction of trichloromethane with hydrogen fluoride; single route, at plant; 3.94 kg/m3, 86.47 g/mol | JP | agg | ts |
Chloroprene (from butadiene via chlorination) from butadiene via chlorination; single route, at plant; 0.96 g/cm3, 88,54 g/mol | US | agg | ts |
Chloroprene (from butadiene via chlorination) from butadiene via chlorination; single route, at plant; 0.96 g/cm3, 88,54 g/mol | EU-28 | agg | ts |
Chromated copper arsenate from chromic acid, copper sulphate and an arsenic compound; single route, at plant; consits of 34% arsenic compound | US | agg | ts |
Chromic acid from sodium dichromate; production mix, at plant; 1.20 g/cm3, 118 g/mol | DE | agg | ts |
Chromic acid anodizing anodizing aluminium in chromic acid solution; single producer, at plant; 1 sqm coated | DE | p-agg | ts |
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, 192.124 g/mol anhydrous, 210.14 g/mol monohydrate | EU-28 | agg | ts |
Clay (self-extraction) (average) Clay extraction; single producer, at plant; 17% moisture | DE | agg | ts |
Clay extracted from clay pit (23.7% moisture) technology mix; production mix, at plant; 23.7% moisture | EU-28 | agg | ts |
Clay extracted from clay pit (23.7% moisture) technology mix; production mix, at plant; 23.7% moisture | AT | agg | ts |
Clay production Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | EU-28 | agg | ts |
Clay production Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | UA | agg | ts |
Clay production Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | BR | agg | ts |
Clay production Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | DE | agg | ts |
Clay production Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | CN | agg | ts |
Clay production (estimation) Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | IN | agg | ts |
Clay production (refractory) open pit mining; single producer, at plant; crude clay | DE | agg | ts |
Clay production mix Clay extraction, mechanical processing and storage; production mix, at plant; 60% H2O content | DE | agg | ts |
Cobalt chloride hexahydrate (estimation) concentrating a HCl solution with CoO; single route, at producer | DE | agg | ts |
Cobalt hydroxide based on cobalt (Ni/Co route) from thinkstep electrolysis of sulphate; production mix, at plant; 3.59 g/cm3, 92.95 g/mol | DE | agg | ts |
Cobalt hydroxide based on cobalt mix from Cobalt Development Institute (CDI) electrolysis of sulphate; production mix, at plant; 3.59 g/cm3, 92.95 g/mol | DE | agg | ts |
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 | ts |
Cobalt mix (only Cu/Co route) Copper cobalt route, hydrometallurgical process; production mix, at plant; 8.90 g/cm3, 58.93 g/mol | GLO | agg | ts |
Cobalt mix (only Ni/Co route) Nickel cobalt route, pyrometallurgical process; production mix, at plant; 8.90 g/cm3, 58.93 g/mol | GLO | agg | ts |
Cobalt, Nickel cobalt route only Nickel cobalt route, pyrometallurgical process; single route, at plant; 8.90 g/cm3, 58.93 g/mol, ferromagnetic | AU | agg | ts |
Coconut cultivation technology mix; production mix, at field border; 48% H2O | PH | p-agg | ts |
Coking coal mix technology mix; consumption mix, at border of producing country; 29 MJ/kg net calorific value | GLO | agg | ts |
Colophony (rosin) from tapped CN living pine, via gum rosin; single route, at plant; gum rosin | EU-28 | agg | ts |
Colophony (rosin) from tapped CN living pine, via gum rosin; production mix, at plant; gum rosin | CN | agg | ts |
Colophony (rosin) from distilled and esterified tall oil resin from distilled and esterified tall oil resin; production mix, at plant; gum rosin | FR | agg | ts |
Colophony (rosin, refined) from CN pine gum rosin from tapped CN living pine, via gum rosin; production mix, at plant; gum rosin | US | agg | ts |
Colophony (rosin, refined) from US pine stump from US pine stump; consumption mix, at plant; gum rosin | US | agg | ts |
Colophony / tall oil resin (estimation from paper production) separation from black liquor, depitching, fatty acid distillation; single route, at plant; gum rosin | US | agg | ts |
Colophony/tall oil resin (estimation from paper production) Kraft pulping, tall oil occurs as by-product; single route, at plant; composition: fatty acids about 42 to 55 %, resin acids about 33 to 47 %, sterines | SE | agg | ts |
Compressed air 1.5 bar (low power consumption) 1.5 bar, high efficiency; consumption mix, at plant; low electricity consumption | GLO | u-so | ts |
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 | ts |
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 | ts |
Compressed air 3.5 bar (low power consumption) 3.5 bar, high efficiency; consumption mix, at plant; low electricity consumption | GLO | u-so | ts |
Compressed natural gas (CNG) technology mix of screw-type and piston compressors; production mix, at plant; compression to 250 bar | EU-28 | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Concrete liquefier (ferrochrome-lignine sulfonate) technology mix; production mix, at plant; Ferrochrome-lignine sulfonate | EU-28 | agg | ts |
Condensed skim milk thermal evaporation using steam heat; production mix, at producer; 65% H2O | US | p-agg | ts |
Connector audio TRS 2.5mm plug (2.0g) (gold-plated) technology mix; production mix, at producer; 2.5mm plug (2.0g) (gold-plated) | GLO | agg | ts |
Connector audio TRS 2.5mm plug (2.0g) (silver-plated) technology mix; production mix, at producer; 2.5mm plug (2.0g) (silver-plated) | GLO | agg | ts |
Connector audio TRS 2.5mm socket (500mg) (gold-plated) technology mix; production mix, at producer; 2.5mm socket (500mg) (gold-plated) | GLO | agg | ts |
Connector audio TRS 2.5mm socket (500mg) (silver-plated) technology mix; production mix, at producer; 2.5mm socket (500mg) (silver-plated) | GLO | agg | ts |
Connector audio TRS 3.5mm plug (3.0g) (gold-plated) technology mix; production mix, at producer; 3.5mm plug (3.0g) (gold-plated) | GLO | agg | ts |
Connector audio TRS 3.5mm plug (3.0g) (nickel-plated) technology mix; production mix, at producer; 3.5mm plug (3.0g) (nickel-plated) | GLO | agg | ts |
Connector audio TRS 3.5mm socket (800mg) (gold-plated) technology mix; production mix, at producer; 3.5mm socket (800mg) (gold-plated) | GLO | agg | ts |
Connector audio TRS 3.5mm socket (800mg) (silver-plated) technology mix; production mix, at producer; 3.5mm socket (800mg) (silver-plated) | GLO | agg | ts |
Connector China type I (38,7 g, 3 pins) technology mix; production mix, at producer; 38,7 g, 3 pins | GLO | agg | ts |
Connector Cinch female (15 g, 1 pin) technology mix; production mix, at producer; 15 g, 1 pin | GLO | agg | ts |
Connector Cinch female (15 g, 1 pin, gold plated) technology mix; production mix, at producer; 15 g, 1 pin, gold plated | GLO | agg | ts |
Connector Cinch male (4,1 g, 1 pin) technology mix; production mix, at producer; 4,1 g, 1 pin | GLO | agg | ts |
Connector Cinch male (4,1 g, 1 pin, gold plated) technology mix; production mix, at producer; 4,1 g, 1 pin, gold plated | GLO | agg | ts |
Connector DC power female (2 g, 1 pin) technology mix; production mix, at producer; 2 g, 1 pin | GLO | agg | ts |
Connector DC power male (2,9 g, 1 pin) technology mix; production mix, at producer; 2,9 g, 1 pin | GLO | agg | ts |
Connector D-Sub (20,4 g, 15 pins, gold plated) technology mix; production mix, at producer; 20,4 g, 15 pins, gold plated | GLO | agg | ts |
Connector D-Sub (21,1 g, 9 pins, gold plated) technology mix; production mix, at producer; 21,1 g, 9 pins, gold plated | GLO | agg | ts |
Connector D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold-plated) technology mix; production mix, at producer; D-sub DE-15 (VGA) 15-pin plug (20.4g) (gold-plated) | GLO | agg | ts |
Connector D-sub DE-15 (VGA) 15-pin socket (8.4g) (gold-plated) technology mix; production mix, at producer; D-sub DE-15 (VGA) 15-pin socket (8.4g) (gold-plated) | GLO | agg | ts |
Connector D-sub DE-9 (RS-232/serial) 9-pin plug (17.7g) (gold-plated) technology mix; production mix, at producer; D-sub DE-9 (RS-232/serial) 9-pin plug (17.7g) (gold-plated) | GLO | agg | ts |
Connector D-sub DE-9 (RS-232/serial) 9-pin socket (7.2g) (gold-plated) technology mix; production mix, at producer; D-sub DE-9 (RS-232/serial) 9-pin socket (7.2g) (gold-plated) | GLO | agg | ts |
Connector HDMI type A (7,9 g, 19 pins, gold plated) technology mix; production mix, at producer; 7,9 g, 19 pins, gold plated | GLO | agg | ts |
Connector HDMI type D (2,7 g, 19 pins, gold plated) technology mix; production mix, at producer; 2,7 g, 19 pins, gold plated | GLO | agg | ts |
Connector HDMI Type-A 19-pin plug (7.8g) (gold-plated) technology mix; production mix, at producer; HDMI Type-A 19-pin plug (7.8g) (gold-plated) | GLO | agg | ts |
Connector HDMI Type-A 19-pin socket (2.0g) (gold-plated) technology mix; production mix, at producer; HDMI Type-A 19-pin socket (2.0g) (gold-plated) | GLO | agg | ts |
Connector HDMI Type-D 19-pin plug (2.7g) (gold-plated) technology mix; production mix, at producer; HDMI Type-D 19-pin plug (2.7g) (gold-plated) | GLO | agg | ts |
Connector IC single-row (2 g, 10 pins) technology mix; production mix, at producer; 2 g, 10 pins | GLO | agg | ts |
Connector IC single-row (2 g, 10 pins, gold plated) technology mix; production mix, at producer; 2 g, 10 pins, gold plated | GLO | agg | ts |
Connector IDC socket (5 g, 40 pins, gold plated) technology mix; production mix, at producer; 5 g, 40 pins, gold plated | GLO | agg | ts |
Connector IEC-60320-C13 female (28,5 g, 3 pins) technology mix; production mix, at producer; 28,5 g, 3 pins | GLO | agg | ts |
Connector IEC-60320-C14 male (9,1 g, 3 pins) technology mix; production mix, at producer; 9,1 g, 3 pins | GLO | agg | ts |
Connector IEC-60320-C5 female (16,8 g, 3 pins) technology mix; production mix, at producer; 16,8 g, 3 pins | GLO | agg | ts |
Connector IEC-60320-C6 male (5,5 g, 3 pins) technology mix; production mix, at producer; 5,5 g, 3 pins | GLO | agg | ts |
Connector IEC-60320-C7 female (5,5 g, 2 pins) technology mix; production mix, at producer; 5,5 g, 2 pins | GLO | agg | ts |
Connector IEC-60320-C8 male (5 g, 2 pins) technology mix; production mix, at producer; 5,5 g, 2 pins | GLO | agg | ts |
Connector Industries 230 V (120 g, 3 pins) technology mix; production mix, at producer; 120 g, 3 pins | GLO | agg | ts |
Connector Industries 400 V (180 g, 5 pins) technology mix; production mix, at producer; 180 g, 5 pins | GLO | agg | ts |
Connector NEMA type A (19,2 g, 2 pins) technology mix; production mix, at producer; 19,2 g, 2 pins | GLO | agg | ts |
Connector NEMA type B (27,7 g, 3 pins) technology mix; production mix, at producer; 27,7 g, 3 pins | GLO | agg | ts |
Connector PATA production of brass pin with gold and nickel coating, production of plastic housing; production mix, at plant; 4 pins | GLO | agg | ts |
Connector PCI (2,6 g, 72 pins, gold plated) technology mix; production mix, at producer; 2,6 g, 72 pins, gold plated | GLO | agg | ts |
Connector power AC mains China Type-I 3-pin plug (38.7g) technology mix; production mix, at producer; China Type-I 3-pin plug (38.7g) | GLO | agg | ts |
Connector power AC mains Euro/Schuko Type-C CEE 7/16 2-pin plug (15g) technology mix; production mix, at producer; Euro/Schuko Type-C CEE 7/16 2-pin plug (15g) | GLO | agg | ts |
Connector power AC mains Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9g) technology mix; production mix, at producer; Euro/Schuko Type-C CEE 7/7 3-pin plug (39.9g) | GLO | agg | ts |
Connector power AC mains industrial 230V 3-pin plug (120g) technology mix; production mix, at producer; industrial 230V 3-pin plug (120g) | GLO | agg | ts |
Connector power AC mains industrial 400V 5-pin plug (180g) technology mix; production mix, at producer; industrial 400V 5-pin plug (180g) | GLO | agg | ts |
Connector power AC mains NEMA Type-A 2-pin plug (19.2g) technology mix; production mix, at producer; NEMA Type-A 2-pin plug (19.2g) | GLO | agg | ts |
Connector power AC mains NEMA Type-B 3-pin plug (27.7g) technology mix; production mix, at producer; NEMA Type-B 3-pin plug (27.7g) | GLO | agg | ts |
Connector power AC mains UK Type-G 3-pin plug (46.5g) technology mix; production mix, at producer; UK Type-G 3-pin plug (46.5g) | GLO | agg | ts |
Connector power DC circular plug (2.9g) technology mix; production mix, at producer; DC circular plug (2.9g) | GLO | agg | ts |
Connector power DC circular socket (2g) technology mix; production mix, at producer; DC circular socket (2g) | GLO | agg | ts |
Connector power IEC-60320-C13 3-pin plug (28.5g) technology mix; production mix, at producer; IEC-60320-C13 3-pin plug (28.5g) | GLO | agg | ts |
Connector power IEC-60320-C14 3-pin socket (10g) technology mix; production mix, at producer; IEC-60320-C14 3-pin socket (10g) | GLO | agg | ts |
Connector power IEC-60320-C5 3-pin plug (17.2g) technology mix; production mix, at producer; IEC-60320-C5 3-pin plug (17.2g) | GLO | agg | ts |
Connector power IEC-60320-C6 3-pin socket (5.5g) technology mix; production mix, at producer; IEC-60320-C6 3-pin socket (5.5g) | GLO | agg | ts |
Connector power IEC-60320-C7 2-pin plug (5.5g) technology mix; production mix, at producer; IEC-60320-C7 2-pin plug (5.5g) | GLO | agg | ts |
Connector power IEC-60320-C8 2-pin socket (5.0g) technology mix; production mix, at producer; IEC-60320-C8 2-pin socket (5.0g) | GLO | agg | ts |
Connector RCA/Cinch plug (4.1g) (gold-plated) technology mix; production mix, at producer; plug (4.1g) (gold-plated) | GLO | agg | ts |
Connector RCA/Cinch plug (4.1g) (silver-plated) technology mix; production mix, at producer; plug (4.1g) (silver-plated) | GLO | agg | ts |
Connector RCA/Cinch socket (2.9g) (gold-plated) technology mix; production mix, at producer; socket (2.9g) (gold-plated) | GLO | agg | ts |
Connector RCA/Cinch socket (2.9g) (silver-plated) technology mix; production mix, at producer; socket (2.9g) (silver-plated) | GLO | agg | ts |
Connector RJ 45 (5,4 g, 8 pins, gold plated) technology mix; production mix, at producer; 5,4 g, 8 pins, gold plated | GLO | agg | ts |
Connector RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-plated) technology mix; production mix, at producer; RJ45/8P8C ethernet 8-pin plug (2.4g) (gold-plated) | GLO | agg | ts |
Connector RJ45/8P8C ethernet 8-pin socket (2.5g) (gold-plated) technology mix; production mix, at producer; RJ45/8P8C ethernet 8-pin socket (2.5g) (gold-plated) | GLO | agg | ts |
Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin plug (5.5g) (gold-plated) technology mix; production mix, at producer; RJ45/8P8C ethernet EMI/RFI shielded 8-pin plug (5.5g) (gold-plated) | GLO | agg | ts |
Connector RJ45/8P8C ethernet EMI/RFI shielded 8-pin socket (3.6g) (gold-plated) technology mix; production mix, at producer; RJ45/8P8C ethernet EMI/RFI shielded 8-pin socket (3.6g) (gold-plated) | GLO | agg | ts |
Connector S-ATA (2 g, 7 pins, gold plated) technology mix; production mix, at producer; 2 g, 7 pins, gold plated | GLO | agg | ts |
Connector SATA 7 + 15 (22-pin) plug (1.4g) (gold-plated) technology mix; production mix, at producer; SATA 7 + 15 (22-pin) plug (1.4g) (gold-plated) | GLO | agg | ts |
Connector Schuko CEE 7/7 (39,9 g, 3 pins) technology mix; production mix, at producer; 39,9 g, 3 pins | GLO | agg | ts |
Connector Steck Klemme Leiste (3 g, 2 pins) technology mix; production mix, at producer; 3 g, 2 pins | GLO | agg | ts |
Connector Steck Rck Einpress Male (4,2 g, 55 pins, gold plated) technology mix; production mix, at producer | GLO | agg | ts |
Connector TRS 2,5 female (10 g, 1 pin) technology mix; production mix, at producer; 10 g, 1 pin | GLO | agg | ts |
Connector TRS 2,5 female (10 g, 1 pin, gold plated) technology mix; production mix, at producer; 10 g, 1 pin, gold plated | GLO | agg | ts |
Connector TRS 2,5 male (2 g, 1 pin, gold plated) technology mix; production mix, at producer; 2 g, 1 pin, gold plated | GLO | agg | ts |
Connector TRS 2,5 male 2 g, 1 pin) technology mix; production mix, at producer; 2 g, 1 pin | GLO | agg | ts |
Connector TRS 3,5 female (15 g, 1 pin) technology mix; production mix, at producer; 15 g, 1 pin | GLO | agg | ts |
Connector TRS 3,5 female (15 g, 1 pin, gold plated) technology mix; production mix, at producer; 15 g, 1 pin, gold plated | GLO | agg | ts |
Connector TRS 3,5 male (2,4 g, 1 pin) technology mix; production mix, at producer; 2,4 g, 1 pin | GLO | agg | ts |
Connector TRS 3,5 male (2,4 g, 1 pin, gold plated) technology mix; production mix, at producer; 2,4 g, 1 pin, gold plated | GLO | agg | ts |
Connector TRS 6,35 female (30 g, 1 pin) technology mix; production mix, at producer; 30 g, 1 pin | GLO | agg | ts |
Connector TRS 6,35 male (20 g, 1 pin) technology mix; production mix, at producer; 20 g, 1 pin | GLO | agg | ts |
Connector TRS 6,35 male (20 g, 1 pin, gold plated) technology mix; production mix, at producer; 20 g, 1 pin, gold plated | GLO | agg | ts |
Connector UK type G (46,5 g, 3 pins) technology mix; production mix, at producer; 46,5 g, 3 pins | GLO | agg | ts |
Connector USB micro (2,5 g, 4 pins, gold plated) technology mix; production mix, at producer; 2,5 g, 4 pins, gold plated | GLO | agg | ts |
Connector USB micro Type-B 5-pin plug (2.5g) (gold-plated) technology mix; production mix, at producer; USB micro Type-B 5-pin plug (2.5g) (gold-plated) | GLO | agg | ts |
Connector USB mini (2,8 g, 4 pins, gold plated) technology mix; production mix, at producer; 2,8 g, 4 pins, gold plated | GLO | agg | ts |
Connector USB mini 5-pin socket (760mg) (gold-plated) technology mix; production mix, at producer; USB mini 5-pin socket (760mg) (gold-plated) | GLO | agg | ts |
Connector USB mini Type-B 5-pin plug (1.1g) (gold-plated) technology mix; production mix, at producer; USB mini Type-B 5-pin plug (1.1g) (gold-plated) | GLO | agg | ts |
Connector USB type A (1,6 g, 4 pins, gold plated) technology mix; production mix, at producer; 1,6 g, 4 pins, gold plated | GLO | agg | ts |
Connector USB type B (8,1 g, 4 pins, gold plated) technology mix; production mix, at producer; 8,1 g, 4 pins, gold plated | GLO | agg | ts |
Connector USB Type-A 4-pin socket (2.1g) (gold-plated) technology mix; production mix, at producer; USB Type-A 4-pin socket (2.1g) (gold-plated) | GLO | agg | ts |
Connector USB Type-B 4-pin plug (10.2g) (gold-plated) technology mix; production mix, at producer; USB Type-B 4-pin plug (10.2g) (gold-plated) | GLO | agg | ts |
Connector USB Type-B 4-pin socket (2.8g) (gold-plated) technology mix; production mix, at producer; USB Type-B 4-pin socket (2.8g) (gold-plated) | GLO | agg | ts |
Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (gold-plated) technology mix; production mix, at producer; wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (gold-plated) | GLO | agg | ts |
Connector wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (tin-plated) technology mix; production mix, at producer; wire-to-board IDC 2.54mm-pitch 2x10 (20-pin) cable-mounted socket (3.3g) (tin-plated) | GLO | agg | ts |
Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (gold-plated) technology mix; production mix, at producer; wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (gold-plated) | GLO | agg | ts |
Connector wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (tin-plated) technology mix; production mix, at producer; wire-to-board pin-header 2.54mm-pitch 2x10 (20-pin) (1.3g) (tin-plated) | GLO | agg | ts |
Copper chloride catalyst (estimation) direct combination of copper and chlorine; single route, at plant; 3.39 g/cm3, 134.45 g/mol | DE | agg | ts |
Copper chloride catalyst (estimation) direct combination of copper and chlorine; single route, at plant; 3.39 g/cm3, 134.45 g/mol | JP | agg | ts |
Copper phthalocyanine phthalic anhydride- urea process; single route, at plant; 1.62 g/cm3, 576.07 g/mol | JP | agg | ts |
Copper phthalocyanine (estimation) phthalic anhydride- urea process; single route, at plant; 1.62 g/cm3, 576.07 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
Copper wire (0.06 mm) wire drawing; single route, at plant; 0.06mm | DE | agg | ts |
Copper wire (0.06 mm) wire drawing; single route, at plant; 0.06mm | EU-28 | agg | ts |
Copper wire (0.6 mm) wire drawing; single route, at plant; 0.6mm | EU-28 | agg | ts |
Cork broken Cork treatment, cork breaking; single route, at plant; 120–240 kg/m3 | DE | agg | ts |
Cork flour Cork washing and grinding; production mix, at plant; grain size ~0,0001mm | DE | agg | ts |
Cork flour (EN15804 A1-A3) Cork washing and grinding; production mix, at plant; grain size ~0,0001mm | EU-28 | agg | ts |
Cork veneer Cork treatment; single route, at plant; 120–240 kg/m3 | DE | agg | ts |
Corrugated board 2015, 84,5% recycled fiber, for use in cut-off EoL technology mix; production mix, at producer; 15,5% primary fibre, 84,5% recycled fibre | EU-28 | p-agg | ts/FEFCO |
Cotton fibre (conventional) cotton ginning; single route, at plant; length of fibers 0.5 inch to 2 inches,1.54–1.56 g/cm³ | US | agg | ts |
Cotton fibre (organic) cotton ginning; single route, at plant; length of fibers 0.5 inch to 2 inches,1.54–1.56 g/cm³ | US | agg | ts |
Cottonseed meal cotton cultivation, seed harvesting, pressing, extraction, refining; single producer, at plant; press cake from cotton oil pressing | US | agg | ts |
Cresol (p-cresol) sulfonation of toluene; single route, at plant; 1.05 g/cm3, 108.14 g/mol | DE | agg | ts |
Crude coconut oil harvest, pressing and extraction; single route, at plant; 80% carbon content | MY | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.3 MJ/kg net calorific value | IR | agg | ts |
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 | ts |
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 | SA | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.1 MJ/kg net calorific value | EC | agg | ts |
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 | MY | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 43.0 MJ/kg net calorific value | MA | agg | ts |
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 | BA | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 41.3 MJ/kg net calorific value | MX | agg | ts |
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 | HR | agg | ts |
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 | US-CA | agg | ts |
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 | OM | agg | ts |
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 | DK | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 43.5 MJ/kg net calorific value | DZ | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.3 MJ/kg net calorific value | IQ | agg | ts |
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 | RU | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 41.3 MJ/kg net calorific value | ID | agg | ts |
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 | KZ | agg | ts |
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 | CH | agg | ts |
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 | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.7 MJ/kg net calorific value | AL | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.3 MJ/kg net calorific value | LK | agg | ts |
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 | RS | agg | ts |
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 | AR | agg | ts |
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 | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.3 MJ/kg net calorific value | PH | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.1 MJ/kg net calorific value | CO | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.8 MJ/kg net calorific value | NG | agg | ts |
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 | CL | agg | ts |
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 | AZ | agg | ts |
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 | CZ | agg | ts |
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 | TM | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.6 MJ/kg net calorific value | SG | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 43.1 MJ/kg net calorific value | AE | agg | ts |
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 | PE | agg | ts |
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 | UZ | agg | ts |
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 | EG | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.6 MJ/kg net calorific value | KR | agg | ts |
Crude oil mix technology mix of conventional and unconventional (oil sands, in-situ) production; consumption mix, to consumer; 42.1 MJ/kg net calorific value | BG | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | CN | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | RU | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | SG | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | TH | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | KR | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | JP | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | TW | agg | ts |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene; production mix, at plant; 0.862 g/cm3, 120.20 g/mol | SA | agg | ts |
Cupric carbonate basic by-product sodium sulphate (estimation) reaction of copper sulphate and sodium carbonate; production mix, at plant; 4 g/cm3, 221 g/mol | EU-28 | agg | ts |
Cyanogen Chloride (via chlorination of hydrocyanic acid) chlorination of hydrocyanic acid; single route, at plant; 61.47 g/mol | DE | agg | ts |
Cyanuric acid pyrolysis of urea; production mix, at plant; 2.5 g/cm3, 129.07 g/mol | DE | agg | ts |
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 | ts |
Cyclododecatriene (CDT, 1,5,9-Cyclododecatriene) cyclotrimerization of butadiene; production mix, at plant; 0.89 g/cm3, 162.28 g/mol | DE | agg | ts |
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 | ts |
Cyclohexanone from cyclohexane; production mix, at plant; 0.95 g/cm3, 98.15 g/mol | DE | agg | ts |
DDGS (from ethanol from corn) Corn dry mill process; single producer, at plant; 26.5% CP | US | agg | ts |
Decabromodiphenyl ethane (estimation) reaction of diphenyl ethane with bromine; single route, at plant; 971.22 g/mol | DE | agg | ts |
Decanoic acid (capric acid) from palm kernel oil (incl. LUC as fossil CO2) (estimate) Enzymatic hydrolysis of palm oil, separation of capric acid; single producer, at plant; density: 0.893 g/cm3, molar mass: 172.26 g mol−1 | EU-28 | agg | ts |
Degreasing agent (aluminium) mixture of soda, tensides, isononanol and water; production mix, at plant; estimation, degreaser | DE | agg | ts |
Deionised water (estimation) via ion exchange; single route, at plant; 1 kg/l, 18 g/mol | MY | agg | ts |
Deionised water (estimation) via ion exchange; single route, at plant; 1 kg/l, 18 g/mol | IN | agg | ts |
Deionised water (estimation) via ion exchange; single route, at plant; 1 kg/l, 18 g/mol | TH | agg | ts |
Deionised water (reverse-osmosis/electrical-deionisation) technology mix, reverse-osmosis/electrical-deionisation; production mix, at plant; 1000 kg/m3, 18 g/mol | CN | agg | ts |
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 | ts |
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 | ts |
Desalinated sea water (Vaporisation, MSF-Plant) vaporisation, multi- stage- flash plant; single route, at plant; 1000 kg/m3, 18 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
Dibenzanthrone alkaline fusion of benzanthrone; production mix, at plant; 1.53 g/cm3, 456.49 g/mol | US | agg | ts |
Dichloromethane chlorination of methyl chloride; production mix, at plant; 1.33 g/cm3, 84.93 g/mol | EU-28 | agg | ts |
Dichloromethane (estimation) chlorination of methyl chloride; production mix, at plant; 1.33 g/cm3, 84.93 g/mol | US | agg | ts |
Dichloropropene by-product allyl chloride (C3H5Cl) chlorination of propene; single route, at plant; 1.16 g/cm3, 112.98 g/mol | DE | agg | ts |
Dichlorotetrafluoroethane (R114) (estimation) from perchloroethylene, hydrogen fluoride and chlorine; production mix, at plant; 1.46 g/cm3, 170.92 g/mol | DE | agg | ts |
Dichlorpropane by-product epichlorohydrin, hydrochloric acid chlorination of propene; single route, at plant; 1.16 g/cm3, 112.98 g/mol | DE | agg | ts |
Dicumyl peroxide (stoichiometric estimation) via cumyl hydroperoxide; single route, at plant; 1.02 g/cm3, 270.37 g/mol | EU-28 | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | NL | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | AU | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | GB | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 350 ppm sulphur | IN | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | EU-28 | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 50 ppm sulphur | MY | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 800 ppm sulphur | CN | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 500 ppm sulphur | BR | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | JP | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | DE | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 15 ppm sulphur | US | agg | ts |
Diesel at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | FR | agg | ts |
Diesel at refinery Western Australia from crude oil; production mix, at refinery; 10 ppm sulphur | AU | agg | ts |
Diesel combustion forest engines diesel- driven forest engine; single operation, at work station; 1 kg diesel combusted | GLO | u-so | ts |
Diesel combustion in construction machine diesel driven | GLO | u-so | ts |
Diesel fuel supplied and combusted in diesel generator technology mix regarding firing and flue gas cleaning; production mix, at diesel generator | EU-28 | agg | ts |
Diesel fuel supplied and combusted in diesel generator (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Diesel fuel supplied and combusted in diesel generator (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Diesel generator mechanical diesel engine; single operation, at work station; >500 kW | GLO | u-so | ts |
Diesel mix at refinery from crude oil and bio components; production mix, at refinery; 10 ppm sulphur, 3.30 wt.% bio components | NL | agg | ts |
Diesel mix at refinery from crude oil and bio components; production mix, at refinery; 350 ppm sulphur, 0.00 wt.% bio components | RU | agg | ts |
Diesel mix at refinery from crude oil and bio components; production mix, at refinery; 50 ppm sulphur, 7.42 wt.% bio components | MY | agg | ts |
Diesel mix at refinery from crude oil and bio components; production mix, at refinery; 10 ppm sulphur, 9.2 wt.% bio components | FR | agg | ts |
Diesel mix at refinery Western Australia from crude oil and bio components; production mix, at refinery; 10 ppm sulphur, 1.26 wt.% bio components | AU | agg | ts |
Diethanolamine (DEA) Reaction of ethylene oxide with excess of ammonia; production mix, at producer; 100% active substance, 1.09 g/cm3, 105.14 g/mol | DE | agg | ts |
Diethyl carbonate (DEC) phosgenation of ethanol; single producer, at plant; 0.975 g/cm3, 118.13 g/mol | DE | agg | ts |
Diethyl ether from ethylene; production mix, at plant; by-product ethanol (96%) | DE | agg | ts |
Diethyl ether (estimation) from ethylene; production mix, at plant; by-product ethanol (96%) | CN | agg | ts |
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 | ts |
Diethylaniline (2,6) from aniline reraction of ethene and aniline; single route, at plant; 0.93 g/cm3, 149.24 g/mol | DE | agg | ts |
Diethyldithiocarbamate from diethyl amine, sodium hydroxide and carbon disulphide; production mix, at plant; 1.1 g/cm3, 171.26 g/mol | DE | agg | ts |
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 | ts |
Diethylene glycol by-product ethylene glycol from ethene and oxygen via EO (estimation) from ethene and oxygen; single route, at plant; 1.12 g/m³, 106 g/mol | SA | agg | ts |
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), at plant; 28% of the energy output is electricity, 72% is steam | EU-28 | p-agg | ts |
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 | ts |
Dimethyl succinate (estimation) 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 | ts |
Dimethyl sulfoxide (from Dimethylsulfide) catalytic oxidation of dimethyl sulfide with oxygen; single router, at plant; 1.10 g/cm3, 78.13 g/mol | DE | agg | ts |
Dimethylamine reaction of methanol and ammonia; production mix, at plant; 0.67 g/cm3, 45.08 g/mol | DE | agg | ts |
Dimethylamine reaction of methanol and ammonia; production mix, at plant; 0.67 g/cm3, 45.08 g/mol | US | agg | ts |
Dimethyldichlorosilane Rochow-Müller-process; single route, at plant; 1.06 g/cm3, 129.06 g/mol | EU-28 | agg | ts |
Dimethyldichlorosilane Rochow-Müller-process; single route, at plant; 1.06 g/cm3, 129.06 g/mol | US | agg | ts |
Dimethylformamide (DMF) (estimation) catalyzed reaction of dimethylamine and carbon monoxide; single route, at plant; 0.948 g/cm3, 73.09 g/mol | DE | agg | ts |
Dimethyloxalate oxidative carbonylation of methanol; single route, at plant; 1.15 g/cm3, 118.09 g/mol | DE | agg | ts |
Dimethylsulphidetoluene diamine (DMTDA) (estimation) reaction of toluene diamine with an organic disulphide; production mix, at plant; 1.21 g/cm3, 214.36 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Dioxothiolane (Sulfolan) from butadiene, via sulfolene; production mix, at plant; 1.26 g/cm3, 120.17 g/mol | DE | agg | ts |
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 | ts |
Diphenyloxide (estimation) non-catalytic process for the production of diphenyloxid and phenylphenol; production mix, at plant; 170.21 g/mol | EU-28 | agg | ts |
Dipropylene glycol from propylene oxide, by product propylene glycol; production mix, at plant; 1.02 g/cm3, 134.17 g/mol | DE | agg | ts |
Dipropyleneglycol dibenzoate plast production from dipropylene glycol and methyl benzoate; production mix, at plant; 342.39 g/mol | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car >2 l biodiesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car >2 l (direct) biodiesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car >2 l (indirect) biodiesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car 1,4-2 l biodiesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car 1,4-2 l (direct) biodiesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by biodiesel (B100) car 1,4-2 l (indirect) biodiesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.3 l CNG driven, Euro 4, passenger car; consumption mix; engine size 1,3l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.3 l (direct) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,3l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.3 l (indirect) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,3l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.6 l CNG driven, Euro 4, passenger car; consumption mix; engine size 1,6l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.6 l (direct) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,6l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.6 l (indirect) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,6l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.9 l CNG driven, Euro 4, passenger car; consumption mix; engine size 1,9l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.9 l (direct) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,9l | EU-28 | agg | ts |
Distance travelled by compressed natural gas (CNG) car 1.9 l (indirect) CNG driven, Euro 4, passenger car; consumption mix; engine size 1,9l | EU-28 | agg | ts |
Distance travelled by diesel car >2 l diesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by diesel car >2 l (direct) diesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by diesel car >2 l (indirect) diesel driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by diesel car 1,4-2 l diesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by diesel car 1,4-2 l (direct) diesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by diesel car 1,4-2 l (indirect) diesel driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by gasoline car <1,4 l gasoline driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by gasoline car <1,4 l (direct) gasoline driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by gasoline car <1,4 l (indirect) gasoline driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by gasoline car >2 l gasoline driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by gasoline car >2 l (direct) gasoline driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by gasoline car >2 l (indirect) gasoline driven, Euro 4, passenger car; consumption mix; engine size more than 2l | EU-28 | agg | ts |
Distance travelled by gasoline car 1,4-2 l gasoline driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by gasoline car 1,4-2 l (direct) gasoline driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by gasoline car 1,4-2 l (indirect) gasoline driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by IC/ EC train (indirect) electricity driven, passenger train; consumption mix; IC/EC train | DE | agg | ts |
Distance travelled by ICE train <200 kmh (indirect) electricity driven, passenger train; consumption mix; ICE train <200 kmh | DE | agg | ts |
Distance travelled by ICE train >200 kmh (indirect) electricity driven, passenger train; consumption mix; ICE train >200 kmh | DE | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l LPG driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l (direct) LPG driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car <1,4 l (indirect) LPG driven, Euro 4, passenger car; consumption mix; engine size up to 1,4l | EU-28 | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l LPG driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (direct) LPG driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by liquified petroleum gas (LPG) car 1,4-2,0 l (indirect) LPG driven, Euro 4, passenger car; consumption mix; engine size 1,4-2l | EU-28 | agg | ts |
Distance travelled by plane (1000 km) (indirect) technology mix, kerosene driven, passenger plane; production mix, at plant; 1000 km | EU-28 | agg | ts |
Distance travelled by plane (250 km) (indirect) technology mix, kerosene driven, passenger plane; production mix, at plant; 250 km | EU-28 | agg | ts |
Distance travelled by plane (500 km) (indirect) technology mix, kerosene driven, passenger plane; production mix, at plant; 500 km | EU-28 | agg | ts |
Distance travelled by plane (5000 km) (indirect) technology mix, kerosene driven, passenger plane; production mix, at plant; 5000 km | EU-28 | agg | ts |
Distance travelled by public bus (indirect) diesel driven, passenger bus; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | DE | agg | ts |
Distance travelled by RE/ RB/ IRE train (indirect) electricity driven, passenger train; consumption mix; RE/ RB/ IRE train | DE | agg | ts |
Distance travelled by truck trailer, 22 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck trailer, 22 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck trailer, 22 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 28 - 34t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 11.4 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 11.4 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 11.4 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 14 - 20t gross weight, 11,4t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 17.3 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 17.3 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 17.3 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 20 - 26t gross weight, 17,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 22 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 22 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 22 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 28 - 32t gross weight, 22t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 24.7 t payload [km] diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 24.7 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 24.7 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, more than 32t gross weight, 24,7t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 3.3 t payload [km] diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 3.3 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 3.3 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, up to 7,5t gross weight, 3,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 5 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 5 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 5 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 7,5 t - 12t gross weight, 5t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 9.3 t payload [km] diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 9.3 t payload [km] (direct) diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Distance travelled by truck, 9.3 t payload [km] (indirect) diesel driven, cargo; consumption mix; Euro 4, 12-14t gross weight, 9,3t payload capacity | EU-28 | agg | ts |
Distance travelled by urban railway (indirect) electricity driven, passenger train; consumption mix; passenger train urban | DE | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | ts |
District cooling (estimation) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NO | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GR | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NL | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CH | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FI | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | LU | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | US | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SE | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | BE | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | HU | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CZ | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SG | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PT | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MX | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MY | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PL | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CA | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AT | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FR | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ES | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | DE | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AE | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GB | agg | ts |
District cooling (estimation) (direct) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | JP | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | JP | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | KZ | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CA | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SE | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NO | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | DE | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CH | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | TR | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | VN | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AE | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | EG | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | BE | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MY | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | NL | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PL | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | AT | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FR | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ID | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | LU | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PT | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | SG | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | HU | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | RS | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | US | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GB | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | PK | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | UA | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | ES | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | CZ | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | GR | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MX | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | MA | agg | ts |
District cooling (estimation) (indirect) pumping cold water, electricity needed for powering pumps; production mix, at plant; COP 3,7 (0.27kWh electricity for 1kWh cooling) | FI | agg | ts |
District heating mix technology mix; production mix, at plant; 10.7 % energy loss during transmission | DE | agg | ts |
District heating mix technology mix; production mix, at plant; 10.7 % energy loss during transmission | CN | agg | ts |
Dolomite (ground) dolomite mining and milling; single route, at plant; 2.90 g/cm3 | DE | agg | ts |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite; production mix, at plant; 2.90 g/cm3 | DE | agg | ts |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite; production mix, at plant; 2.90 g/cm3 | EU-28 | agg | ts |
Dolomite calcination (derived from lime calcination) Decarboxylation process by burning mined dolomite; production mix, at plant; 2.90 g/cm3 | US | agg | ts |
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), at landfill site; wood, natural finish | EU-28 | p-agg | ts |
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 | ts |
Dried quartz sand (grain size 0/2) technology mix; production mix, at plant; grain size 0/2 | EU-28 | agg | ts |
Dried starch (Polyglucose) from corn (economic allocation) corn cultivation and harvesting, wet milling process; single producer, at plant; dried corn starch | EU-28 | agg | ts |
Drum drying (average) Drum drying; single operation, at producer; Drying product on a drum dryer | EU-28 | p-agg | ts |
Drum drying (average) Drum drying; single operation, at producer; Drying product on a drum dryer | US | p-agg | ts |
Dry haricot beans (14% H2O) bean cultivation and harvest; production mix, at field border; 14 % H2O | US | agg | ts |
Dyes mixture of aniline and 2,4-dimethylbenzaldehyde; single producer, at plant; 50% aniline, 50% dimethylbenzaldehyde | DE | agg | ts |
Dysprosium (price allocated) primary production, ore mining and processing, electrolysis; production mix, at plant; 8.56 g/cm3, 162.50 g/mol | CN | agg | ts |
Dysprosium Production (mass allocated) mining and processing, primary production; production mix, at plant; 8.54 g/cm3, 162.50 g/cm3 | CN | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Electricity from diesel fuel (diesel generator) technology mix regarding firing and flue gas cleaning; production mix, at power plant | EU-28 | agg | ts |
Electricity from diesel fuel (diesel generator) (direct) technology mix regarding firing and flue gas cleaning; production mix, at power plant | EU-28 | agg | ts |
Electricity from diesel fuel (diesel generator) (indirect) technology mix regarding firing and flue gas cleaning; production mix, at power plant | EU-28 | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | US | p-agg | ts |
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 | ts |
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 | ts |
Electricity from natural gas via CHP (without supply) 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 | ts |
Electricity from natural gas via direct (without supply) AC, direct combustion, technology mix regarding firing and flue gas cleaning; production mix, at power plant; 1kV - 60kV | US | p-agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | PH | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | IS | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | ID | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at producer; 1kV - 60kV | UA | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | NO | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at producer; 1kV - 60kV | EG | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | PK | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | TH | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | KE | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | MX | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | KR | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | MK | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | SG | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | TW | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | HR | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | LK | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | GLO | agg | ts |
Electricity from photovoltaic AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | IL | agg | ts |
Electricity from photovoltaic (indirect) AC, technology mix of CIS, CdTE, mono crystalline and multi crystalline; production mix, at plant; 1kV - 60kV | DE | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | NG | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | RS | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | LK | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | HK | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | SA | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | BA | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | AE | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | DZ | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | PY | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | SG | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | PK | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | OM | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | VN | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | PH | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | IQ | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | KW | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | MA | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | KZ | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | EG | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | QA | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | KE | agg | ts |
Electricity grid mix AC, technology mix; consumption mix, to consumer; <1kV | IL | agg | ts |
Electricity grid mix - Central AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - Central - 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix - East AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - East - 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix - North AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - North 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix - Northeast AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - Northeast - 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix - Northwest AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - Northwest - 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix - South AC, technology mix; consumption mix, to consumer; <1kV | CN | agg | ts |
Electricity grid mix - South - 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | CN | agg | ts |
Electricity grid mix (average power plants) 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | EU-28 | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | KZ | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | LK | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | ZA | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | HR | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | HK | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | PK | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | VE | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | IQ | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | SG | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | MK | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | RS | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | PH | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | NG | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | KW | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | QA | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | KE | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | SA | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | OM | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | IL | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | PY | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | EG | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | BA | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, at consumer; <1kV | DZ | agg | ts |
Electricity grid mix (direct) AC, technology mix; consumption mix, to consumer; <1kV | MA | agg | ts |
Electricity grid mix (direct) (eGRID) AC, technology mix; consumption mix, at consumer; <1kV | US | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | RS | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | DZ | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | PY | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | IL | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | KE | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | HK | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | VE | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | SA | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | BA | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | IQ | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | PK | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | KZ | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | PH | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | QA | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | MK | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | KW | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | LK | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | OM | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | NG | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | EG | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, at consumer; <1kV | HR | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | SG | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | ZA | agg | ts |
Electricity grid mix (indirect) AC, technology mix; consumption mix, to consumer; <1kV | MA | agg | ts |
Electricity grid mix (indirect) (eGRID) AC, technology mix; consumption mix, at consumer; <1kV | US | agg | ts |
Electricity grid mix 1kV-60kV AC, technology mix; consumption mix, to consumer; 1kV - 60kV | AE | agg | ts |
Electrode baking petrol coke, pitch and hard coal tar; production mix, at plant; >99% carbon | NO | agg | ts |
Electrode baking petrol coke, pitch and hard coal tar; production mix, at plant; >99% carbon | ZA | agg | ts |
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 | ts |
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 | ts |
Electrolytic manganese dioxide (EMD, MnO2) using selenium from manganese ore; production mix, at plant; 5.03 g/cm3, 86.94 g/mol | CN | agg | ts |
Electrolytic manganese dioxide (EMD, MnO2) using SO2 from manganese ore; production mix, at plant; 5.03 g/cm3, 86.94 g/mol | CN | agg | ts |
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 | ts |
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), at plant; 43,0 MJ/kg net calorific value | DE | p-agg | ts |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride; single route, at plant; 1.18 g/cm3, 92.52 g/mol | BE | agg | ts |
Epichlorohydrin (by product calcium chloride, hydrochloric acid) via allyl chloride; single route, at plant; 1.18 g/cm3, 92.52 g/mol | NL | agg | ts |
Epichlorohydrin by-product calcium chloride, hydrochloric acid (estimation) via allyl chloride; single route, at plant; 1.18 g/cm3, 92.52 g/mol | EU-28 | agg | ts |
Epichlorohydrin by-product dichlorpropane, hydrochloric acid chlorination of propene; single route, at plant; 1.18 g/cm3, 92.52 g/mol | DE | agg | ts |
Epichlorohydrin from refined glycerine refined glycerine hydrochlorination to epichlorohydrin; single route, at plant; 1.18 g/cm3, 92.52 g/mol | US | agg | ts |
Epoxidation of soybean oil (ESBO) - open input soy bean (estimation) catalytic epoxidation; production mix, at plant; 0.994 g/cm3 | EU-28 | p-agg | ts |
Epoxidized Methyl Soyate by-prod Glycerine (C mass allocated - estimation) by-product glycerine, soy oil production, refining, transesterification; production mix, at plant; 70,9% carbon content (67,15% bio) | EU-28 | agg | ts |
Epoxised soybean oil (ESBO) (estimation) epoxydising soy bean oil; single route, at plant; 0.994 g/cm3 | EU-28 | agg | ts |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin; production mix, at plant; approx. 1.15 g/cm3 | ES | agg | ts |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin; production mix, at plant; approx. 1.15 g/cm3 | NL | agg | ts |
Epoxy Resin (EP) from Bisphenol A and epichlorohydrin; production mix, at plant; approx. 1.15 g/cm3 | IT | agg | ts |
EPS-Foam (expanded polystyrene foam (PS 12)) incl. flame retardant (estimation) styrene polymerization, foaming; production mix, at plant; PS 12, including flame retardant | US | agg | ts |
Ethane refinery gas separation; single route, at plant; 1.36 g/l, 30.07 g/mol | DE | agg | ts |
Ethane refinery gas separation; single route, at plant; 1.36 g/l, 30.07 g/mol | US | agg | ts |
Ethanol (96%) (catalytic hydrogenation with phosphoric acid) catalytic hydrogenation with phosphoric acid; single route, at plant; 96 % concentrated | DE | agg | ts |
Ethene (ethylene) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | JP | agg | ts |
Ethene (Ethylene) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | MY | agg | ts |
Ethene (ethylene) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | IN | agg | ts |
Ethene (ethylene) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | AU | agg | ts |
Ethene (ethylene) (estimation) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | CN | agg | ts |
Ethene (ethylene) (estimation) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | SA | agg | ts |
Ethene (ethylene) (estimation) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | BE | agg | ts |
Ethene (Ethylene) (Oxi) steam cracker; production mix, at plant; 1.178 kg/m3, 28.05 g/mol | US | agg | ts |
Ethine (acetylene) Sachsse-Bartholome process; production mix, at plant; 1.18 g/l, 26.04 g/mol | GB | agg | ts |
Ethine (acetylene) Sachsse-Bartholome process; production mix, at plant; 1.18 g/l, 26.04 g/mol | EU-28 | agg | ts |
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 | ts |
Ethyl benzene liquid phase alkylation; production mix, at plant; 0.87 g/cm3, 106.17 g/mol | EU-28 | agg | ts |
Ethyl benzene liquid phase alkylation; production mix, at plant; 0.87 g/cm3, 106.17 g/mol | ES | agg | ts |
Ethyl carbonate reaction of ethylene oxide and carbon dioxide; production mix, at plant; 1.32 g/cm3, 88.06 g/mol | DE | agg | ts |
Ethylbenzene (liquid phase alkylation) (estimation) liquid phase alkylation; production mix, at plant; 0.87 g/cm, 106.17 g/mol | IT | agg | ts |
Ethylbenzene (liquid phase alkylation) (estimation) liquid phase alkylation; production mix, at plant; 0.87 g/cm, 106.17 g/mol | BE | agg | ts |
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), at plant; 39,1 MJ/kg net calorific value | EU-28 | p-agg | ts |
Ethylen Propylen Dien Elastomer (EPDM) suspension polymerisation; production mix, at plant; Synthetic rubber | US | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Ethylene (Ethene) via dehydration of ethanol dehydration of ethanol; production mix, at plant; 1.18 kg/m3, 28.05 g/mol | EU-28 | agg | ts |
Ethylene (Ethene) via dehydration of ethanol dehydration of ethanol; production mix, at plant; 1.18 kg/m3, 28.05 g/mol | US | agg | ts |
Ethylene bis(stearamide), EBS (stoichiometric estimation) reaction of ethylene diamine with stearic acid; production mix, at plant; 0.99–1.01 g/cm3, 593.04 g/mol | DE | agg | ts |
Ethylene carbonate via carbon dioxide and ethylene oxide; production mix, at plant; 1.32 g/cm3, 88.06 g/mol | DE | agg | ts |
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 | ts |
Ethylene chlorohydrin (estimation) reaction of ethylene with chlorine and water; single route, at plant; 1.20 g/cm3, 80.51 g/mol | DE | agg | ts |
Ethylene dichloride (EDC) (estimation) from ethene and chlorine; production mix, at plant; 1.25 g/cm3, 98.95 g/mol | EU-28 | agg | ts |
Ethylene dichloride (EDC) (estimation) from ethene and chlorine; production mix, at plant; 1.25 g/cm3, 98.95 g/mol | GB | agg | ts |
Ethylene dichloride (EDC) (estimation) from ethene and chlorine; production mix, at plant; 1.25 g/cm3, 98.95 g/mol | DE | agg | ts |
Ethylene glycol butyl ether via ethylene oxide with butyl alcohol; production mix, at plant; 0.90 g/cm3, 118.18 g/mol | EU-28 | agg | ts |
Ethylene glycol butyl ether via ethylene oxide with butyl alcohol; production mix, at plant; 0.90 g/cm3, 118.18 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Ethylene glycol from ethene and oxygen via EO (estimation) from ethene and oxygen via ethylene oxide; production mix, at plant; 1.11 g/cm³, 62 g/mol | MY | agg | ts |
Ethylene glycol from ethylene oxide from ethene and oxygen via ethylene oxide; production mix, at plant; 1.11 g/cm³, 62 g/mol | DE | agg | ts |
Ethylene Methacrylic Acid Ionomer (EMAA) (high pressure autoclave) copolymerization of of ethylene and methacrylic acid; single producer, at plant | DE | agg | ts |
Ethylene Methyl Acrylate (EMA) copolymerization of ethene and methacrylate; production mix, at plant; 0.94 g/cm3 | DE | agg | ts |
Ethylene Norbornen copolymer (COC, Cyclic olefine copolymers) copolymerization of ethylene and norbornene; single producer, at plant; density 1.02 g/cm³, solid | DE | agg | ts |
Ethylene oxide (EO) by-product carbon dioxide from air purified, oxidation of ethylene with air; production mix, at plant; 0.882 g/mL, 44 g/mol | EU-28 | agg | ts |
Ethylene oxide (EO) by-product ethylene glycol via O2/methane oxidation of ethylene with oxygen; production mix, at plant; 1.93 kg/m3, 44.05 g/mol | EU-28 | agg | ts |
Ethylene oxide (EO) via air oxidation of ethylene with air; production mix, at plant; 1.93 kg/m3, 44.05 g/mol | ES | agg | ts |
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% | EU-28 | agg | ts |
Ethylene Propylene Diene Elastomer (EPDM) copolymerization of ethylene and propylene; production mix, at plant; 0.90 to >2.00 g/cm3 | EU-28 | agg | ts |
Ethylene propylene diene elastomer extrusion profile (EPDM) polymerization of ethylene and propylene, crosslinking, extrusion; single route, at plant; 0.90 to >2.00 g/cm3 | DE | agg | ts |
Ethylene propylene diene elastomer extrusion profile (EPDM) polymerization of ethylene and propylene, crosslinking, extrusion; single route, at plant; 0.90 to >2.00 g/cm3 | EU-28 | agg | ts |
Ethylene tetrafluoroethylene granulate (ETFE) copolymerization reaction of tetrafluoroethylene and ethylene; production mix, at plant; 100.02 g/mol per repeating unit | DE | agg | ts |
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 acetate | DE | agg | ts |
Ethylene vinyl alcohol copolymer (EVOH) hydrolysis of ethylene–vinyl acetate copolymer; single route, at plant; 72 g/mol per repeating unit | DE | agg | ts |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia; single route, at plant; EDA, DETA, TETA, TEPA, PEHA | EU-28 | agg | ts |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia; single route, at plant; EDA, DETA, TETA, TEPA, PEHA | DE | agg | ts |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia; single route, at plant; EDA, DETA, TETA, TEPA, PEHA | US | agg | ts |
Ethyleneamines (EDA, DETA, TETA, TEPA, PEHA) reaction of ethylene dichloride and ammonia; single route, at plant; EDA, DETA, TETA, TEPA, PEHA | GB | agg | ts |
Ethylenediaminetetraacetic acid (EDTA) (estimated) Cyanomethylation of ethylene diamine; single route, at plant; 0.86 g/cm3, 292.24 g/mol | DE | agg | ts |
Ethylene-t-Butylether (ETBE) from C4 reaction of isobutene; single route, at plant; 0.74 g/cm3, 102.18 g/mol | DE | agg | ts |
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 | ts |
Eucalyptus plantation (30% H2O content) perennial cultivation, harvesting, air- drying; single route, at producer; 30% H2O content | BR | agg | ts |
Expanded Polystryrol/polypropylene foam packing (estimation) plasticising and mixing foam; single route, at plant; 70% polystyrene, 30% polypropylene | EU-28 | agg | ts |
Explosives (ANFO) production, explosion; single route, to consumer; blasting agent, explosive; 0.8g/cm3 | EU-28 | agg | ts |
Facade panel (12mm) on landfill landfill including leachate treatment and without collection, transport and pre-treatment; production mix (region specific sites), at landfill site; C 68.8 kg, H 6.2 kg, O 12.3 kg, Si 0.5 kg, inert 912.2 kg | EU-28 | p-agg | ts |
Facade panel (20mm) on landfill landfill including leachate treatment and without collection, transport and pre-treatment; production mix (region specific sites), at landfill site; C 79.3 kg, H 7.0 kg, O 14.1 kg, inert 899.6 kg | EU-28 | p-agg | ts |
Fan HDD (120X25mm, PWM) technology mix; production mix, at plant; 120X25mm, PWM | DE | agg | ts |
Fan PSU (78X25mm, not PWM) technology mix; production mix, at plant; 78X25mm, not PWM | DE | agg | ts |
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 | ts |
Feather meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Feather meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | ZA | agg | ts |
Feather meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Feather meal from poultry (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Feldspar Open-pit mining; Single route, at plant; Al2O3*SiO2*Na2O | US | agg | ts |
Ferric chloride direct chlorination of iron scrap; single route, at plant; estimation, including chlorine recuperation | EU-28 | agg | ts |
Ferric chloride (estimation) direct chlorination of iron scrap; single route, at plant; estimation, including chlorine recuperation | DE | agg | ts |
Ferric oxide (FeO) via Fe2O3 via iron oxide; production mix, at plant; 5.75 g/cm3, 71.85 g/mol | EU-28 | agg | ts |
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 | ts |
Ferrite (MnZn ferrite) shape forming and sintering; single route, at plant; 70% ferrite, 17% manganous oxide, 13% zinc | ES | agg | ts |
Ferro Chrome High Carbon Primary production, ore mining and beneficiation; production mix, at plant; 60 % chrome, high carbon ~ 6% | GLO | agg | ts |
Ferro Chrome Low Carbon Primary production, ore mining and processing; production mix, at plant; 60 % chrome, low carbon ~ 1% | GLO | agg | ts |
Ferromolybdenum mix (Mo 60%) separation, leaching, roasting; production mix, at plant; 60 % molybdenum content | GLO | agg | ts |
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 | ts |
Ferro-Vanadium Primary production, ore mining and processing; production mix, at plant; 80% vanadium content | ZA | agg | ts |
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 | ts |
Fire proof stones (alumina-rich) crushing, mixing, burning; single route, at plant; alumina-rich | CN | agg | ts |
Fire proof stones (alumina-rich) crushing, mixing, burning; single route, at plant; alumina-rich | DE | agg | ts |
Fire proof stones (alumina-rich) crushing, mixing, burning; single route, at plant; alumina-rich | UA | agg | ts |
Fire proof stones (alumina-rich) crushing, mixing, burning; single route, at plant; alumina-rich | BR | agg | ts |
Fire proof stones (alumina-rich) (estimation) crushing, mixing, burning; single route, at plant; alumina-rich | IN | agg | ts |
Fish meal fish grinding, steam cooking, mechanical oil extraction, evaporation; single route, at plant; 20% carbon content, 20 MJ net calorific value | US | agg | ts |
Flat glass Pilkington process, mixing and melting minerals; production mix, at plant; 2500 kg/m3 | DE | agg | ts |
Flax cultivation (10% H2O content) flax cultivation and harvesting; production mix, at field border; 10% H2O content | FR | agg | ts |
Flax seed cultivation (15% H2O content) flax cultivation and harvesting; production mix, at field border; 15% H2O content | CA | agg | ts |
Fluorine electrolysis of KF/HFmixtures; single route, at plant; 1.6965 kg/m3, 37.98 g/mol | DE | agg | ts |
Fluorine electrolysis of KF/HF mixtures; single route, at plant; gas form, 1.6965 kg/m3 at STP condistions (0°C and 1 atm), 37.98 g/mol | EU-28 | agg | ts |
Fluorine (electrolysis hydrogen fluoride) electrolysis of CaF2/HFmixtures; single route, at plant; gas form, 1.6965 kg/m3, 37.98 g/mol | JP | agg | ts |
Fluorine graphite direct fluorination of graphite; production mix, at plant; 31.01 g/mol | JP | agg | ts |
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 | ts |
Fluorosilicic acid by-product phosphoric acid (75%) (estimation) phosphoric acid wet process; single route, at plant; 1.46 g/cm3, 144.09 g/mol | US | agg | ts |
Fluorspar (extraction and processing) extraction and processing; production mix, at plant; 3.2 g/cm3 | MX | agg | ts |
Fluorspar (extraction and processing) extraction and processing; production mix, at plant; 3.2 g/cm3 | DE | agg | ts |
Fluorspar (extraction and processing) extraction and processing; production mix, at plant; 3.2 g/cm3 | US | agg | ts |
Fluorspar (extraction and processing) extraction and processing; production mix, at plant; 3.2 g/cm3 | CN | agg | ts |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning; production mix, at power plant; mineral composition | DE | agg | ts |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning; production mix, at power plant; mineral composition | GB | agg | ts |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning; production mix, at power plant; mineral composition | CN | agg | ts |
Fly ash from hard coal power plant technology mix regarding firing and flue gas cleaning; production mix, at power plant; mineral composition | RO | agg | ts |
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 | ts |
Foam glass 1 cbm from mineral raw materials; production mix, at plant; 1 cbm | EU-28 | p-agg | ts |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol; production mix, at plant; 37 % concentrated | MY | agg | ts |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol; production mix, at plant; 37 % concentrated | EU-28 | agg | ts |
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 | ts |
Freeze drying Freeze drying of food products; single operation, at producer; Production of dried food in a batch process | EU-28 | p-agg | ts |
Freeze drying Freeze drying of food products; single operation, at producer; Production of dried food in a batch process | US | p-agg | ts |
Gadolinium oxide primary production; production mix, at plant; RE95% | US | agg | ts |
Gallium technology mix; production mix, at plant; 5,9 g/cm3 | GLO | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 150 ppm sulphur | RU | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | JP | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 500 ppm sulphur | BR | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 800 ppm sulphur | CN | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 50 ppm sulphur | MY | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | EU-28 | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 30 ppm sulphur | US | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | NL | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | FR | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | GB | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | DE | agg | ts |
Gasoline (premium) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | AU | agg | ts |
Gasoline (premium) at refinery Western Australia from crude oil; production mix, at refinery; 50 ppm sulphur | AU | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 500 ppm sulphur | BR | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 800 ppm sulphur | CN | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 150 ppm sulphur | IN | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | AU | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 150 ppm sulphur | RU | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 30 ppm sulphur | US | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | EU-28 | agg | ts |
Gasoline (regular) at refinery from crude oil; production mix, at refinery; 10 ppm sulphur | JP | agg | ts |
Gasoline (regular) at refinery Western Australia from crude oil; production mix, at refinery; 50 ppm sulphur | AU | agg | ts |
Gasoline (Super) supplied and combusted [gasoline input in kg] Combustion of 1kg fuel input; single route, at plant | EU-28 | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Gasoline mix (premium) at refinery from crude oil and bio components; production mix, at refinery; 10 ppm sulphur, 10.34 wt.% bio components | FR | agg | ts |
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 | ts |
Gasoline mix (premium) at refinery from crude oil and bio components; production mix, at refinery; 10 ppm sulphur, 5.92 wt.% bio components | NL | agg | ts |
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 | ts |
Gasoline mix (premium) at refinery Western Australia from crude oil and bio components; production mix, at refinery; 50 ppm sulphur, 1.38 wt.% bio components | AU | agg | ts |
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 | ts |
Gasoline mix (regular) at refinery Western Australia from crude oil and bio components; production mix, at refinery; 50 ppm sulphur, 1.38 wt.% bio components | AU | agg | ts |
Gelatine from pork skin slaughtering and processing, pig skin via acid treatment; single route, at plant; about 10 % water content | EU-28 | agg | ts |
Generic television manufacturing (TV 65") technology mix; production mix, at producer; 65" Liquid Crystal Display (LCD), Panel Assembly LED TFT, mixed TN-IPS technology, 65" TV Chassis | GLO | agg | ts |
Glass fibre fleece (21% UF resin) (estimation) mixing of glass fiber, UF and PMMA, fleece production; production mix, at plant; 21% urea formaldehyde resin | DE | agg | ts |
Glass fibre mesh technology mix; production mix, at plant; Glass fibre | CN | agg | ts |
Glass fibre mesh technology mix; production mix, at plant; Glass fibre | EU-28 | agg | ts |
Glass fibres from mineral components; production mix, at plant; Borosillicate glass / E-glass | UA | agg | ts |
Glass fibres from mineral components; production mix, at plant; Borosillicate glass / E-glass | CN | agg | ts |
Glass fibres from mineral components; production mix, at plant; Borosillicate glass / E-glass | EU-28 | agg | ts |
Glass fleece from glass fibres and urea- formaldehyde- resin; production mix, at plant; 82% glass fibres and 18% UF resin | CN | agg | ts |
Glass fleece from glass fibres and urea- formaldehyde- resin; production mix, at plant; 82% glass fibres and 18% UF resin | UA | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Glue system mixing different adhesives; production mix, at plant; 33% casein glue, 33% phenol resorcin resin, 33% polyurethane | DE | agg | ts |
Glycerin 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 | ts |
Glycerine (from Epichlorohydrine) via epichlorohydrine; single route, at plant; 1.26 g/cm3, 92.09 g/mol | BE | agg | ts |
Glycerine (from Epichlorohydrine) via epichlorohydrine; single route, at plant; 1.26 g/cm3, 92.09 g/mol | NL | agg | ts |
Glycerine (from Epichlorohydrine) via epichlorohydrine; single route, at plant; 1.26 g/cm3, 92.09 g/mol | ES | agg | ts |
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 | NL | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Glycerol ester from balm colophony esterification of glycerine with retinoic acid; single route, at plant; 376 g/mol | EU-28 | agg | ts |
Glycerol ester from balm colophony esterification of glycerine with retinoic acid; single route, at plant; 376 g/mol | DE | agg | ts |
Glycidylmethacrylate esterification of methacrylic acid with epichlorohydrin; single route, at plant; 1.04 g/cm3, 142.15 g/mol | DE | p-agg | ts |
Glycidylmethacrylate esterification of methacrylic acid with epichlorohydrin; single route, at plant; 1.04 g/cm3, 142.15 g/mol | EU-28 | agg | ts |
Glycidylmethacrylate esterification of methacrylic acid with epichlorohydrin; single route, at plant; 1.04 g/cm3, 142.15 g/mol | DE | agg | ts |
Glycidylmethacrylate (estimation) esterification of methacrylic acid with epichlorohydrin; single route, at plant; 1.04 g/cm3, 142.15 g/mol | US | agg | ts |
Grey cast iron (GGG70) part (chill-mold) reduction in blast furnace, chill- mold; single route, at plant; GGG70 | DE | p-agg | ts |
Gypsum (CaSO4 alpha hemihydrate from FGD gypsum) grinded and purified product, via calcination of calcium sulphate dihydrate; production mix, at plant; 145.15 g/mol | CN | agg | ts |
Gypsum (CaSO4 alpha hemihydrate from FGD gypsum) grinded and purified product, via calcination of calcium sulphate dihydrate; production mix, at plant; 145.15 g/mol | UA | agg | ts |
Gypsum (CaSO4 alpha hemihydrate from FGD gypsum) grinded and purified product, via calcination of calcium sulphate dihydrate; production mix, at plant; 145.15 g/mol | BR | agg | ts |
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 | ts |
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 | ts |
Gypsum plaster (CaSO4-Beta-hemihydrate) (from 100% gypsum stone) gypsum stone extraction, grinding and calcination; Mandatory:single route, at plant; 145.15 g/mol | DE | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | ES | agg | ts |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining; production mix, at plant; grinded and purified product | CN | agg | ts |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining; production mix, at plant; grinded and purified product | UA | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | MX | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | TR | agg | ts |
Gypsum stone (CaSO4-Dihydrate) underground and open pit mining; production mix, at plant; grinded and purified product | BR | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | CA | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | SA | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | JP | agg | ts |
Gypsum stone (CaSO4-Dihydrate) open pit mining; single route, at plant; 172 g/mol | US | agg | ts |
Gypsum stone (CaSO4-Dihydrate) (EN15804 A1-A3)) underground and open pit mining; production mix, at plant; grinded and purified product | EU-28 | agg | ts |
Hard coal supplied and combusted in power plant technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Hard coal supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Hard coal supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
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 | ts |
Hardwood log mix forest cultivation, harvesting, wet storage; production mix, at plant; 50% timber beech, 50% timber oak | DE | agg | ts |
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 | ts |
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 | ts |
Heavy Fuel Oil (HFO) supplied and combusted in power plant technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Heavy Fuel Oil (HFO) supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Heavy Fuel Oil (HFO) supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil; production mix, at refinery; 1 wt.% sulphur | RU | agg | ts |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil; production mix, at refinery; 1 wt.% sulphur | NL | agg | ts |
Heavy fuel oil at refinery (1.0 wt.% S) from crude oil; production mix, at refinery; 1 wt.% sulphur | MY | agg | ts |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil; production mix, at refinery; 2.5 wt.% sulphur | RU | agg | ts |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil; production mix, at refinery; 2.5 wt.% sulphur | NL | agg | ts |
Heavy fuel oil at refinery (2.5wt.% S) from crude oil; production mix, at refinery; 2.5 wt.% sulphur | MY | agg | ts |
Helium (liquid) Collins cycle (compression, precooling and expansion in different stages); single producer, at plant; boiling point of He -269°C | DE | agg | ts |
Hemp straw cultivation (10% H2O content) hemp cultivation; production mix, at field border; 10% H2O content | DE | agg | ts |
Hemp straw with catch crop hemp cultivation with catch crop; production mix, at field border; 12% H2O content | DE | agg | ts |
Hemp with catch crop hemp cultivation with catch crop; production mix, at field border; 15% H2O content | DE | agg | ts |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine; single route, at plant; 643.71 g/mol | CN | agg | ts |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine; single route, at plant; 643.71 g/mol | US | agg | ts |
Hexamethylene diamine (HMDA) from butadiene via dichlorobutene from butadiene; single route, at plant; 0.84 g/cm3, 116.20 g/mol | FR | agg | ts |
Hexamethylene diamine (HMDA) over adiponitrile HMDA via hydrogenation of adiponitrile; single route, at plant; 0.84 g/mL, 116.20 g/mol | FR | agg | ts |
Hexamethylene diamine (HMDA) via adipic acid HMDA via adipic acid; single route, at plant; 0.84 g/mL, 116.20 g/mol | BE | agg | ts |
Hexamethylene diamine (HMDA) via Adiponitrile (from Acrylonitrile) HMDA via hydrogenation of adiponitrile; single route, at plant; 0.84 g/mL, 116.20 g/mol | US | agg | ts |
Hexamethylene diamine (HMDA) via adiponitrile (from butadiene) from butadiene; single route, at plant; 0.84 g/cm3, 116.20 g/mol | US | agg | ts |
Hexamethylene diisocyanate (HMDI) by-product HCl from hexamethylenediamine (HDI) by phosgenation; single route, at plant; 1.047 g/cm3, 168 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile) HMDA via hydrogenation of adiponitrile; single route, at plant; 0.84 g/mL, 116.20 g/mol | DE | agg | ts |
Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile) HMDA via hydrogenation of adiponitrile; single route, at plant; 0.84 g/mL, 116.20 g/mol | EU-28 | agg | ts |
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 | ts |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene via adiponitrile; single route, at plant; 0.84 g/mL, 116.20 g/mol | EU-28 | agg | ts |
Hexamethylenimin by-product HMDA via adipic acid by- product HMDA, via adipic acid; single route, at plant; 0.88 g/cm3, 99.17 g/mol | DE | agg | ts |
Hexanediol diglycidyl ether (estimation) coupling process; single route, at plant; 230.3 g/mol | EU-28 | agg | ts |
Hexanediol diglycidyl ether (estimation) coupling process; single route, at plant; 230.3 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
High performance film (polypropylene/polyethylene membrane/foil) Plastic extruding, melting, casting and mechanical forming; single route, at plant; 1.08 g/cm3 | DE | agg | ts |
High performance film (polyvinyl butyral) Plastic extruding, melting, casting and mechanical forming; single route, at plant; 1.08 g/cm3 | DE | agg | ts |
High performance film (PVB, LCP, Polyacrylate, PEEK, PEI, Polyethersulfide) Plastic extruding, melting, casting and mechanical forming; single producer, at plant; PVB, LCP, Polyacrylate, PEEK, PEI, Polyethersulfide | DE | p-agg | ts |
Hominy (nixtamal, estimation) intensive cultivation, conventional nixtamization process; production mix, at plant; 12% moisture content | US | agg | ts |
Hydrazine hydrate/hydrazine Bayer Ketazine Process; production mix, at plant; 1.02 g/cm3, 32.05 g/mol | DE | agg | ts |
Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl) reaction of chlorine and propene; single route, at plant; 100% HCl | EU-28 | agg | ts |
Hydrochloric acid (100%) by-product allyl chloride (C3H5Cl) reaction of chlorine and propene; single route, at plant; 100% HCl | MY | agg | ts |
Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride; single route, at plant; 100% HCl | DE | agg | ts |
Hydrochloric acid (100%) by-product epichlorohydrine, calcium chloride from Epichlorhydrin synthesis, by-product epichlorohydrine, calcium chloride; single route, at plant; 100% HCl | MY | agg | ts |
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 | ts |
Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane; single route, at plant; 100% HCl | MY | agg | ts |
Hydrochloric acid (100%) by-product epichlorohydrine, dichloro propane from Epichlorhydrin synthesis, by-product epichlorohydrine, dichloro propane; single route, at plant; 100% HCl | DE | agg | ts |
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 | ts |
Hydrochloric acid (32%), by-product Methylene diisocyanate (MDI), methanol phosgenation of methylenedianiline; single route, at plant; 32% concentrated | DE | agg | ts |
Hydrochloric acid (32%), by-product Methylene diisocyanate (MDI), methanol phosgenation of methylenedianiline; single route, at plant; 32% concentrated | BE | agg | ts |
Hydrochloric acid (phosgenation) by-product toluene diamine (TDA),toluene diisocyanate phosgenation of toluene diamine; single producer, at plant; 32 % concentrated | GB | agg | ts |
Hydrochloric acid 100% (primarily from chlorine) combustion of hydrogen with chlorine; production mix, at plant; 100% HCl | DE | agg | ts |
Hydrochloric acid 100% (primarily from chlorine) combustion of hydrogen with chlorine; production mix, at plant; 100% HCl | CN | agg | ts |
Hydrochloric acid 100% (primarily from chlorine) (estimation) combustion of hydrogen with chlorine; production mix, at plant; 100% HCl | IN | agg | ts |
Hydrochloric acid 32% primarily from chlorine; production mix, at plant; 32 % concentrated | JP | agg | ts |
Hydrochloric acid by-product methylene diisocyanate (MDI), methanol phosgenation of methylenedianiline; single route, at plant; 32% concentrated | FR | agg | ts |
Hydrogen (chlorine-alkali-electrolysis, membrane) from chlorine-alkali electrolysis (membrane); single route, at plant; 0.0899 kg/m3, 2 g/cm3 | EU-28 | agg | ts |
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 value | EU-28 | agg | ts |
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 value | EU-28 | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | GB | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | IN | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | JP | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | BR | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | CN | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | FR | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | DE | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | EU-28 | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | AU | agg | ts |
Hydrogen at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Hydrogen cyanide (prussic acid, Andrussow process) Andrussow process; production mix, at plant; 0.687 g/cm3, 27.03 g/mol | US | agg | ts |
Hydrogen cyanide (prussic acid, BMA process) BMA process; single route, at plant; 0.687 g/cm3, 27.03 g/mol | DE | agg | ts |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate ammoxidation of propene; single route, at plant; 0.687 g/cm3, 27.03 g/mol | EU-28 | agg | ts |
Hydrogen cyanide by-product acrylonitrile (AN), ammonium sulphate ammoxidation of propene; single route, at plant; 0.687 g/cm3, 27.03 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
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 | ts |
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 | NL | agg | ts |
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 | ts |
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 | ts |
Hydrogen sulphide reaction of hydrogen and sulphur; single route, at plant; 1.36 g/l, 34.08 g/mol | EU-28 | agg | ts |
Hydrolysis resistant coating (estimation) hydrolysis resistant coating; single route, at plant; 60 g/m2 | EU-28 | p-agg | ts |
Hydrolysis resistant coating (estimation) hydrolysis resistant coating; single route, at plant; 60 g/m2 | US | p-agg | ts |
Hydrotreated Vegetable oil (HVO) from beef tallow remdering, tallow processing, transport, pretreatment, hydroprocessing; single route, at plant; 780 kg/m3, 44 MJ/kg net calorific value | FI | agg | ts |
Hydrotreated Vegetable oil (HVO) 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 | ts |
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 | ts |
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 | ts |
Hydroxybenzoic acid alkali phenoxide route; single producer, at plant; density 1.46 g/cm³, 138.121 g/mol | EU-28 | agg | ts |
Hydroxybenzoic acid alkali phenoxide route; single producer, at plant; density 1.46 g/cm³, 138.121 g/mol | DE | agg | ts |
Hydroxyethylenemethacrylate reaction of methacrylic acid and ethylene oxide; single route, at plant; 1.07 g/cm3, 130.14 g/mol | DE | agg | ts |
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), at plant; Municipal waste incineration | DE | agg | ts |
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), at plant; Municipal waste incineration | EU-28 | agg | ts |
Industrial wood mix (20% H2O content) Forest cultivation, plantation maintanance; production mix, at producer (different trees); Mix of spruce-, beech-, -oak and pinewood, 20% water content, 14.65 MJ/kg net calorific value | EU-28 | agg | ts |
Iodine pentafluoride (estimation) direct fluorination of molten iodine; single route, at producer; 221.89 g/mol, 3.25 g/cm3 | US | agg | ts |
Ion exchange resin (estimation) sulfonation of polystyrene; single route, at plant; 0.801 g/cm3 | DE | agg | ts |
Ion exchange resin (estimation) sulfonation of polystyrene; single route, at plant; 0.801 g/cm3 | US | agg | ts |
Ionomeres copolymerization of of ethylene and methacrylic acid; single route, at plant; 0.95 g/cm3 | DE | agg | ts |
Iron ore-mix iron ore mining and processing; import mix, to consumer; 5.00 g/cm3, 231.53 g/mol | CN | agg | ts |
Iron ore-mix iron ore mining and processing; import mix, to consumer; 5.00 g/cm3, 231.53 g/mol | JP | agg | ts |
Iron ore-mix iron ore mining and processing; import mix, to consumer; 5.00 g/cm3, 231.53 g/mol | DE | agg | ts |
Iron oxide (Fe2O3) dissolving iron ore in acid; single route, at plant; 5.24 g/cm3, 159.70 g/mol | CN | agg | ts |
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 | ts |
Iron oxide (ferrite) (Fe2O3) electrolytical; single route, at plant; 5.24 g/cm3, 159.70 g/mol | DE | agg | ts |
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 | ts |
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 | ts |
Isophorone diisocyanate (IPDI) from acetone; single route, at plant; 1.06 g/cm3, 222.3 g/mol | EU-28 | agg | ts |
Isophorone diisocyanate (IPDI) from acetone; single route, at plant; 1.06 g/cm3, 222.3 g/mol | DE | agg | ts |
Isopropanol indirect hydrogenation; single route, at plant; 0.78 g/cm3, 60.10 g·/mol | BE | agg | ts |
Jatropha oil Jatropha cultivation, fruit harvest, transport, processing of seeds, oil extraction; single route, at plant; 37 MJ net calorific value | IN | agg | ts |
Kaolin mining, wet processing, drying and grinding; single route, at plant; 2.16- 2.68 g/cm3 | CN | agg | ts |
Kerosene / Jet A1 at refinery from crude oil; production mix, at refinery; 400 ppm sulphur | NL | agg | ts |
Kerosene / Jet A1 at refinery from crude oil; production mix, at refinery; 0.2 wt.% sulphur | MY | agg | ts |
Kerosene / Jet A1 at refinery from crude oil; production mix, at refinery; 0.2 wt.% sulphur | RU | agg | ts |
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 | ts |
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 | ts |
Kerosene supplied and combusted [Kerosene input in kg] Combustion of 1kg fuel input; single route, at plant | EU-28 | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Lactic acid (homofermentative) fermentation of carbohydrates; single route, at plant; 90.08 g/mol | EU-28 | agg | ts |
Lactic acid (homofermentative) - open input corn seeds fermentation of carbohydrates; single route, at plant; 90.08 g/mol | DE | p-agg | ts |
Lactose monohydrate (estimation) milk pretreatment, processing of curd and whey, ultrafiltration, reverse osmosis filtration, crystallisation, centrifugation, spray drying; production mix, at plant; 40% carbon content | DE | agg | ts |
L-alanine preparation (fermentation) (estimation) highly concentrated powder, via fermentation, estimation; single route, at plant; 1.42 g/cm3, 89.09 g/mol | CN | p-agg | ts |
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-PVB-Gorilla laminate thickness: 0.7 mm glass x 0.76 mm PVB interlayer x 0.7 mm glass | US | agg | ts |
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 glass-PVB- flat glass laminate thickness: 1.6 mm glass x 0.76 mm PVB interlayer x 1.6 mm glass | EU-28 | agg | ts |
Landfilling of food waste (according to the WARM model) treatment of leachate, production of electricity from percentage of landfill gas captured; production mix (region specific sites), at landfill site; MSW, Municipal Solid Waste treatment | US | p-agg | ts |
Lanthan-Nickel5 (LaNi5, 88% lanthan, 12% nickel) mixing lanthan and nickel; consumer mix, to consumer; 88% lanthan, 12% nickel | EU-28 | agg | ts |
Laughing gas ammmonium nitrate route; single route, at plant; 1.85 kg/m3, 44.01 g/mol | DE | agg | ts |
Lead battery 12V (estimation) assembling housing, electrodes and electrolyte; production mix, at plant; 12V | DE | agg | ts |
Lead oxide (Barton Pot, estimation) Barton Pot Process, oxidation of lead with air; single route, at plant; 9.53 g/cm3, 223.19 g/mol | EU-28 | agg | ts |
Lead stearate (stabilizer, estimation) reaction of stearic acid and lead oxide; single producer, at plant; 1.4 g/cm3, 774.15 g/mol | EU-28 | agg | ts |
Leather (unvarnished; 1 sqm/0.88 kg) estimation of technology for the use in automotive industry; production mix, at plant; 1 sqm, unvarnished | DE | agg | ts |
Leather (unvarnished; 1 sqm/0.88 kg) - open input cattle hide, open energy inputs estimation of technology for the use in automotive industry; production mix, at plant; 1 sqm, unvarnished | DE | p-agg | ts |
Leather coating (PU) spray coating of leather with polyurethane polyacrylate dispersion; single route, at plant; 1 kg of leather coated | EU-28 | p-agg | ts |
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 | ts |
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 | ts |
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 | ts |
Leather hang drying (Split leather) Hang drying; single route, at plant; 1 kg dried leather | EU-28 | p-agg | ts |
Leather retanning & finishing (aldehyde tanned; Split leather) after aldehyde tanning; single route, at plant; 1 kg, average waste water | EU-28 | p-agg | ts |
Leather retanning & finishing (chromium tanned; Split leather) Post-tanning/finishing after chrome tanning, average waste water emissions; single route, at plant; 1 kg | EU-28 | p-agg | ts |
Leather vacuum drying - open input wet blue leather vacuum drying; single route, at plant; 0.48% H2O for dried hide | EU-28 | p-agg | ts |
Leather vacuum drying - open input wet blue leather vacuum drying; single route, at plant; 0.48% H2O for dried hide | US | p-agg | ts |
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 | ts |
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 | ts |
Light Fuel Oil (LFO) supplied and combusted in power plant technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Light Fuel Oil (LFO) supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Light Fuel Oil (LFO) supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Light fuel oil at refinery from crude oil; production mix, at refinery; 0.3 wt.% sulphur | RU | agg | ts |
Light fuel oil at refinery from crude oil; production mix, at refinery; 0.1 wt.% sulphur | NL | agg | ts |
Light fuel oil at refinery from crude oil; production mix, at refinery; 0.3 wt.% sulphur | MY | agg | ts |
Lignite dust grinding lignite; production mix, at plant; 21.5 MJ net calorific value | EU-28 | agg | ts |
Lignite dust grinding lignite; production mix, at plant; 21.5 MJ net calorific value | DE | agg | ts |
Lignite dust (estimation) grinding lignite; production mix, at plant; 21.5 MJ net calorific value | IN | agg | ts |
Lime (CaO) grinding grinding; production mix, at plant; 3.34 g/cm3, 56.08 g/mol | UA | agg | ts |
Lime (CaO) grinding grinding; production mix, at plant; 3.34 g/cm3, 56.08 g/mol | EU-28 | agg | ts |
Lime (CaO) grinding grinding; production mix, at plant; 3.34 g/cm3, 56.08 g/mol | DE | agg | ts |
Lime (CaO) grinding grinding; production mix, at plant; 3.34 g/cm3, 56.08 g/mol | CN | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | TH | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | NL | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | MY | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | CN | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | UA | agg | ts |
Lime (CaO; quicklime lumpy) from limestone; production mix, at plant; 3.37 g/cm3, 56.08 g/mol | BR | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | DE | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | EU-28 | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | UA | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | CN | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | BR | agg | ts |
Lime hydrate (Ca(OH)2) slaking lime hydrate slaking; production mix, at plant; 2.24 g/cm3, 74.10 g/mol | NL | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | NL | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | BR | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | CN | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | EU-28 | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | TH | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | UA | agg | ts |
Limestone (CaCO3; washed) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | AU | agg | ts |
Limestone (CaCO3; washed) (estimation) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | RU | agg | ts |
Limestone (CaCO3; washed) (estimation) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | GB | agg | ts |
Limestone (CaCO3; washed) (estimation) mining and benefication; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | IN | agg | ts |
Limestone flour (0.115mm) limestone mining and beneficiation; production mix, at producer; grain size 0.115mm | DE | agg | ts |
Limestone flour (0.115mm) limestone mining and beneficiation; production mix, at producer; grain size 0.115mm | EU-28 | agg | ts |
Limestone flour (0.12mm) limestone mining and beneficiation; production mix, at plant; grain size 0.12mm | DE | agg | ts |
Limestone flour (0.12mm) limestone mining and beneficiation; production mix, at producer; grain size 0.12mm | EU-28 | agg | ts |
Limestone flour (0.17mm) limestone mining and beneficiation; production mix, at plant; grain size 0.17mm | DE | agg | ts |
Limestone flour (0.17mm) limestone mining and beneficiation; production mix, at producer; grain size 0.17mm | EU-28 | agg | ts |
Limestone flour (0.1mm) limestone mining and beneficiation; production mix, at producer; grain size 0.1mm | EU-28 | agg | ts |
Limestone flour (0.25mm) limestone mining and milling; production mix, at plant; grain size 0.25mm | CN | agg | ts |
Limestone flour (0.25mm) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | EU-28 | agg | ts |
Limestone flour (0.25mm) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | DE | agg | ts |
Limestone flour (0.25mm) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | UA | agg | ts |
Limestone flour (0.25mm) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | BR | agg | ts |
Limestone flour (0.25mm) (estimation) limestone mining and milling; production mix, at plant; grain size 0.25mm | IN | agg | ts |
Limestone flour (0.25mm) (estimation) limestone mining and milling; production mix, at plant; grain size 0.25mm | BR | agg | ts |
Limestone flour (0.25mm) (estimation) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | TH | agg | ts |
Limestone flour (0.25mm) (estimation) limestone mining and beneficiation; production mix, at plant; grain size 0.25mm | RU | agg | ts |
Limestone flour (0.3mm) limestone mining and beneficiation; production mix, at plant; grain size 0.3mm | DE | agg | ts |
Limestone flour (0.3mm) limestone mining and beneficiation; production mix, at producer; grain size 0.3mm | EU-28 | agg | ts |
Limestone flour (0.5mm) limestone mining and beneficiation; production mix, at producer; grain size 0.5mm | EU-28 | agg | ts |
Limestone flour (0.75mm) limestone mining and beneficiation; production mix, at producer; grain size 0.75mm | EU-28 | agg | ts |
Limestone flour (0.75mm) limestone mining and beneficiation; production mix, at plant; grain size 0.75mm | DE | agg | ts |
Limestone flour (0.7mm) limestone mining and beneficiation; production mix, at producer; grain size 0.7mm | EU-28 | agg | ts |
Limestone flour (0.7mm) limestone mining and beneficiation; production mix, at plant; grain size 0.7mm | DE | agg | ts |
Limestone flour (1.25mm) limestone mining and beneficiation; production mix, at producer; grain size 1.25mm | EU-28 | agg | ts |
Limestone flour (1.25mm) limestone mining and beneficiation; production mix, at plant; grain size 1.25mm | DE | agg | ts |
Limestone flour (1.75mm) limestone mining and beneficiation; production mix, at plant; grain size 1.75mm | DE | agg | ts |
Limestone flour (1.75mm) limestone mining and beneficiation; production mix, at producer; grain size 1.75mm | EU-28 | agg | ts |
Limestone flour (1.82mm) limestone mining and beneficiation; production mix, at producer; grain size 1.82mm | EU-28 | agg | ts |
Limestone flour (1.82mm) limestone mining and beneficiation; production mix, at plant; grain size 1.82mm | DE | agg | ts |
Limestone flour (12µm) limestone mining and beneficiation; production mix, at producer; grain size 12µm | EU-28 | agg | ts |
Limestone flour (12µm) limestone mining and beneficiation; production mix, at plant; grain size 12µm | DE | agg | ts |
Limestone flour (2.15mm) limestone mining and beneficiation; production mix, at plant; grain size 2.15mm | DE | agg | ts |
Limestone flour (2.15mm) limestone mining and beneficiation; production mix, at producer; grain size 2.15mm | EU-28 | agg | ts |
Limestone flour (2.25mm) limestone mining and beneficiation; production mix, at producer; grain size 2.25mm | EU-28 | agg | ts |
Limestone flour (2.25mm) limestone mining and beneficiation; production mix, at plant; grain size 2.25mm | DE | agg | ts |
Limestone flour (25µm) limestone mining and beneficiation; production mix, at producer; grain size 25µm | EU-28 | agg | ts |
Limestone flour (25µm) limestone mining and beneficiation; production mix, at plant; grain size 25µm | DE | agg | ts |
Limestone flour (29µm) limestone mining and beneficiation; production mix, at producer; grain size 29µm | EU-28 | agg | ts |
Limestone flour (29µm) limestone mining and beneficiation; production mix, at plant; grain size 29µm | DE | agg | ts |
Limestone flour (30µm) limestone mining and beneficiation; production mix, at plant; grain size 30µm | DE | agg | ts |
Limestone flour (30µm) limestone mining and beneficiation; production mix, at producer; grain size 30µm | EU-28 | agg | ts |
Limestone flour (46µm) limestone mining and beneficiation; production mix, at plant; grain size 46µm | DE | agg | ts |
Limestone flour (46µm) limestone mining and beneficiation; production mix, at producer; grain size 46µm | EU-28 | agg | ts |
Limestone flour (50µm) limestone mining and beneficiation; production mix, at producer; grain size 50µm | EU-28 | agg | ts |
Limestone flour (7µm) limestone mining and beneficiation; production mix, at producer; grain size 7µm | EU-28 | agg | ts |
Limestone flour (7µm) limestone mining and beneficiation; production mix, at plant; grain size 7µm | DE | agg | ts |
Limestone flour (CaCO3; dried) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | AU | agg | ts |
Limestone flour (CaCO3; dried) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | UA | agg | ts |
Limestone flour (CaCO3; dried) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | EU-28 | agg | ts |
Limestone flour (CaCO3; dried) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | BR | agg | ts |
Limestone flour (CaCO3; dried) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | CN | agg | ts |
Limestone flour (CaCO3; dried) (estimation) milling and drying; production mix, at plant; 2.73 g/cm3, 100.09 g/mol | IN | agg | ts |
Liquefied Petroleum Gas (LPG) from conventional natural gas production; production mix, at producer | EU-28 | agg | ts |
Liquefied Petroleum Gas (LPG) from conventional natural gas production; production mix, at producer | NL | agg | ts |
Liquefied Petroleum Gas (LPG) from conventional natural gas production; production mix, at producer | AU | agg | ts |
Liquefied Petroleum Gas (LPG) from conventional natural gas production; production mix, at producer | RO | agg | ts |
Liquefied Petroleum Gas (LPG) from conventional natural gas production; production mix, at producer | GB | agg | ts |
Liquefied Petroleum Gas (LPG), from conventional natural gas production from conventional natural gas production; production mix, at producer | US | agg | ts |
Liquefied Petroleum Gas (LPG), from shale gas production from shale gas production; production mix, at producer | US | agg | ts |
Liquid carbon dioxide electric- driven compression of gaseous carbon dioxide; production mix, at plant; 60 bar pressure | US | agg | ts |
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 | ts |
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 | ts |
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 | ts |
Lithium carbonate (from brine) extraction from brine; production mix, at plant; 2.11 g/cm3, 73.89 g/mol | CL | agg | ts |
Lithium carbonate (spodumene route) (with credits) spodumene route; production mix, at plant; 2.11 g/cm3, 73.89 g/mol | CN | agg | ts |
Lithium Carbonate mix technology mix; production mix, at plant; 2.11 g/cm3, 73.89 g/mol | GLO | agg | ts |
Lithium carbonate mix (brine) extraction from brine; production mix, at plant; 2.11 g/cm3, 73.89 g/mol | GLO | agg | ts |
Lithium carbonate mix (spodumene) spodumene route; production mix, at plant; 2.11 g/cm3, 73.89 g/mol | GLO | agg | ts |
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 | ts |
Lithium cobalt oxide battery cell (LiCoO2, LCO), 100g cell weight technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 100g, housing weight 10g, capacity 5100 mAh | CN | agg | ts |
Lithium cobalt oxide battery cell (LiCoO2, LCO), scaled up to 1 kg production of battery components, battery assembling; production mix, at plant; 1 kg, 55.25 Ah capacity | GLO | agg | ts |
Lithium Hexafluorophosphate (LiPF6) reaction of lithium fluoride and phosphorous pentafluoride; production mix, at plant; 1.5 g/cm3, 151.9 g/mol | JP | agg | ts |
Lithium iron phosphate battery cell (LiFePO4), 100g cell weight technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 100g, housing weight 10g, capacity 5800 mAh | CN | agg | ts |
Lithium mangan oxide battery cell (LiMn2O4, Spinell), 100g cell weight technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 100g, housing weight 10g, capacity 4220 mAh | CN | agg | ts |
Lithium manganese oxide sintering lithium carbonate and manganous oxide; production mix, at plant; 2.93 g/cm3 | JP | agg | ts |
Lithium metal (high Na-concentration) electrolysis of lithium chloride (LiCl); single route, at plant; 0.534 g/cm3, 6.94 g/mol | DE | agg | ts |
Lithium metal (low Na-concentration) electrolysis of lithium chloride (LiCl); single route, at plant; 0.534 g/cm3, 6.94 g/mol | DE | agg | ts |
Lithium metal (low Na-concentration) electrolysis of lithium chloride (LiCl); single route, at plant; 0.534 g/cm3, 6.94 g/mol | US | agg | ts |
Lithium nickel cobalt manganese oxide battery (NMC), 100 kg weight, without housing technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 100 kg, housing weight 6.99 kg, capacity 15 kWh | GLO | p-agg | ts |
Lithium nickel cobalt manganese oxide battery cell (NMC), 100g cell weight technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 100g, housing weight 10g, capacity 5980 mAh | CN | agg | ts |
Lithium nickel cobalt manganese oxide battery cell (NMC), 40g cell weight technology mix of electrode production, stacking, packaging and filling/ sealing; production mix, at plant; cell weight 40g, housing weight 4g, capacity 2400 mAh | DE | agg | ts |
Lithium sulfide from lithium carbonate and hydrogen sulphide (estimation) from reaction of lithium carbonate with hydrogen sulfide; single route, at producer; 45.95 g/mol | EU-28 | agg | ts |
Lithium sulfide from lithium hydroxide (estimation) from reaction of lithium hydroxide with hydrogen sulfide; single route, at producer; 45.95 g/mol | JP | agg | ts |
Lithium sulfide from lithium hydroxide (estimation) from reaction of lithium hydroxide with hydrogen sulfide; single route, at producer; 45.95 g/mol | DE | agg | ts |
Lithium sulfide from lithium metal (estimation) from reaction of lithium metal with sulfur; single route, at producer; 45.95 g/mol | DE | agg | ts |
Lithium sulfide from lithium metal (estimation) from reaction of lithium metal with sulfur; single route, at producer; 45.95 g/mol | JP | agg | ts |
Lithium sulfide from lithium sulphate and carbon black (estimation) from reaction of lithium sulphate with carbon black; single route, at producer; 45.95 g/mol | EU-28 | agg | ts |
Lithium titanate (Li4Ti5O12) technology mix, sol gel method and hydrothermal synthesis; production mix, at plant; 459 g/mol | GLO | agg | ts |
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 | ts |
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 | ts |
Lubricants at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Lubricants at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Magnesium oxide (MgO, calcinate, fillers) Dolomite preparation, calcination; single route, at plant; 3.58 g/cm3, 40.30 g/mol | DE | agg | ts |
Magnesium oxide (MgO, calcinate, fillers) Dolomite preparation, calcination; single route, at plant; 3.58 g/cm3, 40.30 g/mol | EU-28 | agg | ts |
Magnesium oxide (MgO, fine, filler) calcining magnesium carbonate; single route, at plant; 3.58 g/cm3, 40.30 g/mol | DE | agg | ts |
Magnesium oxide (MgO, fine, filler) calcining magnesium carbonate; single route, at plant; 3.58 g/cm3, 40.30 g/mol | EU-28 | agg | ts |
Magnesium sulphate (agrarian) (economic allocation) from carnallitic hard salt; single route, at plant; 2.66 g/cm3, 120.366 g/mol | EU-28 | agg | ts |
Magnet Nd-Fe-Dy-B sintered magnet process; single route, at plant; energy density >385 kJ/m³ | DE | agg | ts |
Magnet Nd-Fe-Dy-B sintered magnet process; single route, at plant; energy density >385 kJ/m³ | CN | agg | ts |
Maize cultivation, whole plant (72.6% H2O content) technology mix; production mix, at field border; 72.6% H2O | DE | agg | ts |
Manganese sulphate (estimation) manganese dissolved in sulphuric acid; single route, at plant; 3.25 g/cm3, 151.00 g/mol | DE | agg | ts |
Manufacturing electric motor (<=10kW) assembling electric motor; production mix, at plant; <=10kW | EU-28 | agg | ts |
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 | ts |
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 | ts |
Marble (granulation 30 µm) limestone mining and beneficiation; production mix, at plant; grain size 30 µm | DE | agg | ts |
Marble (granulation 30 µm) limestone mining and beneficiation; production mix, at plant; grain size 30 µm | CN | agg | ts |
Marble (granulation 30 µm) limestone mining and beneficiation; production mix, at plant; grain size 30 µm | UA | agg | ts |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Meat and bone meal (MBM) from cattle (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Meat and bone meal (MBM) from pig (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Meat and bone meal (MBM) from pig (economic allocation) (estimation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | RU | agg | ts |
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 | ts |
Melamine Stami carbon process; production mix, at plant; 1.57 g/cm3, 126.12 g/mol | EU-28 | agg | ts |
Melamine foam melamine- formaldehyde addition, etherification with alcohol (foaming); single route, at plant; 14 MJ/ kg net calorific value | DE | agg | ts |
Metal Glue (Screw sealing) components mixing; single route, at plant; 20% succinic acid dibutyl ester, 70% glycidylmethacrylate, 10% silica sand | EU-28 | agg | ts |
Methanol from natural gas from natural gas; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | IT | agg | ts |
Methanol from natural gas from natural gas; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | GB | agg | ts |
Methanol from natural gas from natural gas; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | NL | agg | ts |
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 | ts |
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 | ts |
Methanol from natural gas (combined reforming) from natural gas; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | JP | agg | ts |
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 | ts |
Methanol from natural gas (combined reforming) from natural gas; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | NO | agg | ts |
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 | ts |
Methanol from natural gas (combined reforming) estimate from natural gas, combined reforming; production mix, at plant; 0.79 g/cm3, 32.04 g/mol | CN | agg | ts |
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 | ts |
Methanthiol (methyl mercaptan) reaction of methanol and hydrogen sulphide; production mix, at plant; 2.00 kg/m3, 48.11 g/mol | EU-28 | agg | ts |
Methionine from ammonia; single route, at plant; 149.21 g/mol | BR | agg | ts |
Methionine from ammonia; single route, at plant; 149.21 g/mol | US | agg | ts |
Methoxypropylacetate PGMEA (estimation) esterification of propylene glycol monomethyl ether with acetic acid; production mix, at plant; 0.96 g/cm³, 132.2 g/mol | DE | agg | ts |
Methyl cellulose via alkali cellulose; production mix, at plant; 0.25- 0.7 g/cm3 | DE | agg | ts |
Methyl isobutyl ketone (MIBK) from acetone and hydrogen; single route, at plant; 0.80 g/cm3, 100.16 g/mol | EU-28 | agg | ts |
Methylamine (by-product di-, trimethylamine) via methanol and ammonia; production mix, at plant; 31.06 g/mol | EU-28 | agg | ts |
Methylamine by-product di-, trimethylamine via methanol and ammonia; production mix, at plant; 31.06 g/mol | DE | agg | ts |
Methyldiethanolamine (MDEA) reaction of ethylene oxide and monomethylamine; production mix, at plant; 1.04 g/cm3, 119.16 g/mol | DE | agg | ts |
Milk protein concentrate powder (from skim milk) (MPC 70) via spray drying; production mix, at producer; MPC 70 | US | agg | ts |
Milk protein concentrate powder (from skim milk) (MPC 70) (4% moisture, 1% fat) via spray drying; production mix, at producer; MPC 70 | US | agg | ts |
Milk protein concentrate powder (from skim milk) (MPC 70) (fat allocation) via spray drying; production mix, at producer; MPC 70 | US | agg | ts |
Milk protein concentrate powder 4424 (MPC 70) via spray drying; production mix, at producer; MPC 4424 | US | agg | ts |
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 | ts |
Molasse from sugar beet washing, shredding, extraction, sterilization, juice purification and concentration, crystallization; production mix, at plant; beet molasses, 20% H2O | EU-28 | agg | ts |
Molasse from sugar cane by-product from crystall sugar production; single route, at plant; 20% H2O | TH | agg | ts |
Molasse from sugar cane (45% burning) by-product from crystall sugar production; single route, at plant; 20% H2O | BR | agg | ts |
Molded pulp loose from bagasse integrated plant case (estimation) pulp blending, molding, drying; single route, at plant; energy for the process from bagasse combustion | CN | agg | ts |
Molded pulp loose from bagasse stand alone plant case (estimation) pulp blending, molding, drying; single route, at plant; energy for the process from natural gas and electricity grid | CN | agg | ts |
Molybdenum flotation, roasting, reduction; production mix, at plant; 10.28 g/cm3 | GLO | agg | ts |
Monocalciumphosphate (MCP; for Feed) (estimation) from burnt chalk and phosphoric acid; single route, at plant; 252.05 g/mol | EU-28 | agg | ts |
Monocalciumphosphate (MCP; for Feed) (estimation) from burnt chalk and phosphoric acid; single route, at plant; 252.05 g/mol | GLO | agg | ts |
Mozzarella manufacturing curd production, spinning+ stretching, molding, cooling and salting; single producer, at plant; from curd | US | agg | ts |
Nafion (estimation) production from TFE and a sulfonyl fluoride; production mix, at plant | US | agg | ts |
N-Alkyl asparagine aciddiester (estimation) reaction of succinic acid with ammonia, esterification of the aspartic acid; production mix, at plant; 192 g/mol for aspartic acid diethyl ester | DE | agg | ts |
Naphtha at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Naphtha at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Naphtha at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Naphtha at refinery (estimated) from crude oil; production mix, at refinery; refinery operations are based on US; upstream processes, i.e. crude oil mix, natural gas mix and electricity, are Venezuelan specific | VE | agg | ts |
Natural gas (via LNG) from Australia technology mix; consumption mix, at consumer; medium pressure level (< 1 bar) | KW | agg | ts |
Natural Gas (via LNG) from Qatar technology mix; consumption mix, at consumer; medium pressure level (< 1 bar) | KW | agg | ts |
Natural gas mix technology mix; consumption mix, to consumer; medium pressure level (< 1 bar) | AE | agg | ts |
Natural Gas Mix (2030) technology mix; consumption mix, to consumer; medium pressure level (< 1 bar) | EU-28 | agg | ts |
Natural gas supplied and combusted in gas turbine technology mix regarding firing and flue gas cleaning; production mix, at plant | EU-28 | agg | ts |
Natural gas supplied and combusted in gas turbine (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Natural gas supplied and combusted in gas turbine (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Natural gas supplied and combusted in power plant technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Natural gas supplied and combusted in power plant (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Natural gas supplied and combusted in power plant (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | agg | ts |
Natural graphite (estimation) mining and beneficiation; production mix, at plant; 2.1- 2.3 g/cm3 | GLO | agg | ts |
Natural gypsum mix (including imports) open pit mining; production mix, at plant; 172 g/mol | US | agg | ts |
Natural rubber latex collecting from rubber tree, rubber processing; single producer, at plant; 930 kg/m3, 45.2 MJ kg net calorific value | TH | agg | ts |
Natural soda trona mining, milling, calcination, purification; single route, at plant; 2.53 g/cm3, 105.99 g/mol | US | agg | ts |
Needle-punched non-woven - open input fibre spundbonding process; single route, at plant; 1 kg woven fabric | US | p-agg | ts |
Needle-punched non-woven - open input fibre spundbonding process; single route, at plant; 1 kg woven fabric | EU-28 | p-agg | ts |
Neodymium primary production, ore mining and processing, electrolysis; production mix, at plant; 7.00 g/cm3, 144.24 g/cm3 | CN | agg | ts |
Neodymium oxide primary production; production mix, at plant; RE95% | CN | agg | ts |
Nepheline Production Open-pit and underground mining, transport; import mix, to consumer; 2.55- 2.66 g/cm3 | US | agg | ts |
Nepheline Production Open-pit and underground mining, transport; import mix, to consumer; 2.55- 2.66 g/cm3 | NO | agg | ts |
Nepheline Production Open-pit and underground mining, transport; import mix, to consumer; 2.55- 2.66 g/cm3 | DE | agg | ts |
Nickel cadmium battery - 0,98 kg, estimation, material composition average product based on literature review; production mix, at plant; 1.2V nominal cell voltage | GLO | agg | ts |
Nickel hydroxide electrolysis of sulphate; production mix, at plant; 4.10 g/cm3, 92.72 g/mol | DE | agg | ts |
Nickel nitrate hexahydrate (estimation) dissolving nickel metal in nitric acid; production mix, at plant; 2.05 g/cm3, 290.79 g/mol | DE | agg | ts |
Nitrile butadiene rubber (NBR) fiber, fiber production estimated with vulcanisation Emulsion polymerization of acrylonitrile and butadiene, vulcanisation and fibration; production mix, at plant; 23% acrylonitrile content | DE | agg | ts |
Nitrobenzene from benzene via nitration; production mix, at plant; 1.199 g/cm3, 123.06 g/mol | EU-28 | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | RO | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | IN | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | CN | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | AU | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | CZ | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | PL | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | TH | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | HU | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | CH | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | MY | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | SE | agg | ts |
Nitrogen (gaseous) via cryogenic air separation; production mix, at plant; 1.250 kg/m3, 14.0 g/mol | JP | agg | ts |
Nitrogen (liquid) via cryogenic air separation; production mix, at plant; 14.0 g/mol | AU | agg | ts |
Nitrogen (liquid) via cryogenic air separation; production mix, at plant; 14.0 g/mol | EU-28 | agg | ts |
Nitrogen (liquid) via cryogenic air separation; production mix, at plant; 14.0 g/mol | CN | agg | ts |
Nitrogen (liquid) via cryogenic air separation; production mix, at plant; 14.0 g/mol | TH | agg | ts |
n-Methylpyrolidone (NMP, butyrolactone over butandiol) butyrolactone over butandiol; single route, at plant; 1.03 g/cm3, 99.13 g/mol | DE | agg | ts |
n-Methylpyrolidone mix (NMP) technology mix, butyrolactone from maleic anhydride and butandiol; production mix, at producer; 1.03 g/cm3, 99.13 g/mol | DE | agg | ts |
Oat cultivation, Fife Scotland (17% H2O content) technology mix; production mix, at field border; 17% H2O | GB | agg | ts |
Oat cultivation, West Sussex, England (14% H2O content) technology mix; production mix, at field border; 14% H2O | GB | agg | ts |
ODD Laptop technology mix; production mix, at plant; ODD | GLO | agg | ts |
ODD PC technology mix; production mix, at plant; ODD | GLO | agg | ts |
Olive oil (virgin) olive cultivation, two phase extraction; production mix, at plant; carbon content 77% | EU-28 | agg | ts |
Olive oil (virgin) olive cultivation, two phase extraction; production mix, at plant; carbon content 77% | ES | agg | ts |
Oxygen (gaseous) via cryogenic air separation; production mix, at plant; 1.429 kg/m3, 16.0 g/mol | TW | agg | ts |
Oxygen (gaseous) via cryogenic air separation; production mix, at plant; 1.429 kg/m3, 16.0 g/mol | AU | agg | ts |
Oxygen (gaseous) via cryogenic air separation; production mix, at plant; 1.429 kg/m3, 16.0 g/mol | IN | agg | ts |
Oxygen (gaseous) via cryogenic air separation; production mix, at plant; 1.429 kg/m3, 16.0 g/mol | JP | agg | ts |
Oxygen (gaseous) via cryogenic air separation; production mix, at plant; 1.429 kg/m3, 16.0 g/mol | CN | agg | ts |
Oxygen (highly pure, liquid) via cryogenic air separation, highly pure; production mix, at plant; 16.0 g/mol | US | agg | ts |
Oxygen (liquid) via cryogenic air separation; production mix, at plant; 16.0 g/mol | SE | agg | ts |
Oxygen (liquid) via cryogenic air separation; production mix, at plant; 16.0 g/mol | EU-28 | agg | ts |
Oxytriazol from semicarbazide hydrochloride and formic acid; single route, at plant; 83 g/mol | EU-28 | agg | ts |
PA 6.6 GF thermal break transport, extrusion, mixing, injection moulding, thermal break composition; production mix, at plant; contains glass fibres | EU-28 | agg | ts |
PA6.6GF30 injection molding part (estimation) plastic injection molding; production mix, at plant; 30% glass fibres | MY | agg | ts |
Palladium chloride reaction of palladium, chlorine and aqua regia; production mix, at plant; 4.0 g/cm3, 177.3 g/mol | GLO | agg | ts |
Patchouli Oil technology mix; production mix, at plant | EU-28 | agg | ts |
PBT in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; Municipal waste incineration | DE | p-agg | ts |
PBT in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; Municipal waste incineration | EU-28 | p-agg | ts |
PE Non-woven fabric (estimation) spundbonding process; single route, at producer; estimation | DE | agg | ts |
Pellet-feed-mix (import mix) Beneficiation, pelletizing, sintering; consumer mix, to consumer; concentrated- ore pellets | DE | agg | ts |
Perchloroethylene via hydrochloric acid recycling; production mix, at plant; 1.62 g/cm3, 165.82 g/mol | DE | agg | ts |
PET fabric (flame laminated) in waste inceneration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant | DE | p-agg | ts |
PET fabric (fleece laminated) in waste inceneration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant | DE | p-agg | ts |
PET fleece (1 sqm) plastic production, weaving; single producer, at plant; 1 sqm | DE | agg | ts |
PET knitted fabric (knitted backscrim; 1 sqm) - open input PET fiber knitting; single route, at plant; 1 sqm | DE | p-agg | ts |
Petroleum coke at refinery from crude oil; production mix, at refinery; 31 MJ/kg net calorific value | NL | agg | ts |
Petroleum coke at refinery from crude oil; production mix, at refinery; 31 MJ/kg net calorific value | RU | agg | ts |
Petroleum coke at refinery from crude oil; production mix, at refinery; 31 MJ/kg net calorific value | MY | agg | ts |
Phenol formaldehyde (33% glass beads, 20% glass fibres) polycondensation of phenol and formaldehyde, mixing with glass and filler; production mix, at plant; 33% glass beads, 20% glass fibres | EU-28 | agg | ts |
Phenol formaldehyde (55% glas beads, 10% MD) polycondensation of phenol and formaldehyde, mixing with glass and filler; production mix, at plant; 55% glass beads, 10% talcum filler | EU-28 | agg | ts |
Phenol formaldehyde resin polycondensation in acidic/ caustic medium, resin drying; production mix, at plant; Resol syrup 50% solid | DE | agg | ts |
Phenol formaldehyde-resin (Novolac) polycondensation of phenol and formaldehyde; production mix, at plant; incl. wood flake filler (40% wood content) | EU-28 | agg | ts |
Phosgene (COCl2) continuous process, via chlorine and carbon monoxide; single route, at plant; 4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol | BE | agg | ts |
Phosgene (COCl2) continuous process, via chlorine and carbon monoxide; single route, at plant; 4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol | DE | agg | ts |
Phosgene (COCl2) continuous process, via chlorine and carbon monoxide; single route, at plant; 4.25 g/L at 15 °C, 1.43 g/cm3 at 0 °C, 98.92 g/mol | US | agg | ts |
Phosphorus ore mining/processing/transport to EU (raw phosphorus) mining, processing and transportation to Europe; consumption mix, to consumer; 30% phosphorus pentoxide | CN | agg | ts |
Phosphorus ore mining/processing/transport to EU (raw phosphorus) mining, processing and transportation to Europe; consumption mix, to consumer; 30% phosphorus pentoxide | RU | agg | ts |
Phosphorus oxychloride (POCl3) (estimate) via phosphorus trichloride; single route, at plant; 1.65 g/cm3, 153.33 g/mol | DE | agg | ts |
Pigment (red) condensation of an ester with an aromatic amine, aftertreatment with solvent; single route, at plant; 1.47 g/cm³ | DE | agg | ts |
Plastic foil (Polyethylene, PE) Plastic production, extruding and calendering; production mix, at plant; gauge of about 0.1 to 0.5 mm | DE | agg | ts |
Plastic foil (Polyethylene, PE) Plastic production, extruding and calendering; production mix, at plant; gauge of about 0.1 to 0.5 mm | CN | agg | ts |
Plastic granulate secondary (non specific) from post-consumer plastic waste, via grinding, metal separation, washing, pelletization; single route, at plant; nonspecific plastic waste, without metal fraction | DE | p-agg | ts |
Plastic granulate secondary (non specific, no metal contamination) from post-consumer plastic waste, via grinding, metal separation, washing, pelletization; single route, at consumer; plastic waste without metal fraction | EU-28 | p-agg | ts |
Plastic granulate secondary (nonspecific, low burden) from post-consumer plastic waste, via grinding, metal separation, washing, pelletization; single route, at plant; nonspecific plastic waste, low burden | EU-28 | p-agg | ts |
Plastic granulate secondary (PET) from PET waste; production mix, at plant; 82% recycling rate | DE | p-agg | ts |
Poly(ethylene-alt-maleic anhydride) / Ethylene-maleic anhydride copolymer suspension polymerization; single route, at producer; estimation, alternating copolymer | DE | agg | ts |
Polyacrylamide (anionic) (solid) copolimerization of acrylic acid and acrylamide; single route, at plant; 71,08 g·mol−1 per repeating unit | DE | agg | ts |
Polyacrylamide (cationic), powder Solution polymerization, extrusion and granulation; single route, at plant; 71,08 g·mol−1 per repeating unit | DE | agg | ts |
Polyacrylate ink (estimation) mixing basic chemicals; single route, at plant; 59% acrylate, 38% dipropylenglycole, 3% benzene | DE | agg | ts |
Polyacrylate ink (estimation) mixing basic chemicals; single route, at plant; 59% acrylate, 38% dipropylenglycole, 3% benzene | US | agg | ts |
Polyacrylate primary dispersion 40% emulsion polymerization; single producer, at plant; dispersion 40% | DE | agg | ts |
Polyacrylate primary dispersion 40% emulsion polymerization; single producer, at plant; dispersion 40% | EU-28 | agg | ts |
Polyacrylic acid (PAA) polymerization of acrylic acid; single route, at plant; 1.4 g/cm3 | EU-28 | agg | ts |
Polyacrylic acid (PAA) polymerization of acrylic acid; single route, at plant; 1.4 g/cm3 | DE | agg | ts |
Polyacrylonitrile Fibres (PAN) Polymerization, dissolving, spinning; single route, at plant; PAN without additives, 53 g/mol | DE | agg | ts |
Polyalphaolefine over 1-Decen (PAO) oligomerization and hydogenation of decene; single producer, at plant | DE | agg | ts |
Polyamid (PA) 6 in waste incineration plant (25% inert) waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; 25% inert | DE | p-agg | ts |
Polyamide (PA) 12 (incl. 20% TiO2) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; Net calorific value 29 MJ/kg | EU-28 | agg | ts |
Polyamide (PA) 12 (incl. 20% TiO2) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; Net calorific value 29 MJ/kg | EU-28 | p-agg | ts |
Polyamide (PA) 6.10 granulate secondary (biobased) from post-consumer biobased plastic waste, via grinding, metal separation, washing, pelletization; single route, at consumer; plastic waste without metal fraction | DE | p-agg | ts |
Polyamide 6 fibers (PA 6) spinning of polyamide and epoxy resin; production mix, at plant | DE | agg | ts |
Polyamide 6 Granulate (PA 6) reaction of caprolactam with water; production mix, at plant; 1.084 g/cm3, 113 g/mol per repeating unit | CH | agg | ts |
Polyamide 6.10 Granulate (PA 6.10) (HMDA via adipic acid, CN sebacic acid (worst case)) HMDA via adipic acid, CN sebaccic acid (worst case); single route, at consumer; PA 6.10 granulate | DE | agg | ts |
Polyamide 6.10 Granulate (PA 6.10) (HMDA via adiponitrile, CN sebacic acid (best case)) HMDA via adiponitrile, CN sebaccic acid (best case); single route, at consumer; estimation | DE | agg | ts |
Polyamide 6.6 fibers (PA 6.6) (HMDA over AN) spinning of polyamide and epoxy resin; production mix, at plant; 1.13- 1.14 g/cm3 | DE | agg | ts |
Polyamide 6.6 Granulate (PA 6.10) (HMDA via adipic acid, CN sebacic acid (worst case)) HMDA via adipic acid, CN sebacic acid (worst case); single route, at producer; estimation | DE | agg | ts |
Polyamide 6.6 Granulate (PA 6.10) (HMDA via adiponitrile, CN sebacic acid (best case)) HMDA via adiponitrile, CN sebacic acid (best case); single route, at producer; estimation | DE | agg | ts |
Polyamide 6.6 granulate (PA 6.6) (HMDA over AN) from hexamethylene diamine and adipic acid; production mix, at plant; 1.14 g/cm3, 226.32 g/mol per repeating unit | EU-28 | agg | ts |
Polyamide 6.6 granulate (PA 6.6) (HMDA over AN) from hexamethylene diamine and adipic acid; production mix, at plant; 1.14 g/cm3, 226.32 g/mol per repeating unit | FR | agg | ts |
Polyamide PA 6.6 adhesive continuous process extrusion; single route, at plant; estimation, filler CaCO3 | DE | agg | ts |
Polybutylene succinate (PBS) (biobased from corn) technology mix, starch hydrolysis, fermentation, filtration, esterification, polycondensation; production mix, at producer; from US corn, water content <0,5 w% | EU-28 | agg | ts |
Polycarbonate-acrylonitrile-butadiene-styrene compound (80% PC, 20% ABS) mixing, pelletizing and compounding; single route, at plant; 80% polycarbonate, 20% acrylonitrile- butadiene- styrene | DE | agg | ts |
Polyethylene (PE; 15% H2O content) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant | EU-28 | p-agg | ts |
Polyethylene Film (PE-LD) without additives Polymerisation of ethylene, extruding and calendering; production mix, at plant; 0.91- 0.96 g/cm3, 28.05 g/mol per repeating unit | EU-28 | agg | ts |
Polyethylene glycol (PEG) ring-opening polymerization of ethylene oxide; single route, at plant; 44 g/mol | DE | agg | ts |
Polyethylene glycol (PEG) ring-opening polymerization of ethylene oxide; single route, at plant; 44 g/mol | EU-28 | agg | ts |
Polyethylene high density granulate (HDPE/PE-HD) (biobased from sugar cane) production of biobased ethylene from bioethanol, polymerisation; single route, at plant; 0.91- 0.96 g/cm3, 28 g/mol per repeating unit | US | agg | ts |
Polyethylene high density granulate (HDPE/PE-HD) (biobased from sugar cane) from biobased ethylene based on BR sugar cane (45% slash and burn); production mix, at plant; 0.91- 0.96 g/cm3, 28 g/mol per repeating unit | BR | agg | ts |
Polyethylene high density granulate (HDPE/PE-HD) (biobased from wheat) production of biobased ethylene from bioethanol, polymerisation; single route, at plant; 0.91- 0.96 g/cm3, 28 g/mol per repeating unit | US | agg | ts |
Polyethylene terephthalate (PET) fibres (bottle grade) (biobased) partially biobased via terephthalic acid and ethylene glycol from biobased ethylene based on sugar cane; single route, at producer; Ethylene glycol biobased and terephthalic acid fossil based, PET fibres without additives | EU-28 | agg | ts |
Polyethylene terephthalate fiber from r-PET granulation, washing, pelletizing, spinning; single route, at plant; r-PET fibre | DE | p-agg | ts |
Polyethylene terephthalate granulate (PET via DMT) (partially biobased from sugar cane) from dimethyl terephthalate and biobased ethylene glycol; production mix, at plant; 1.38 g/cm3, 192.17 g/mol | EU-28 | agg | ts |
Polyimide Polycondensation of maleic anhydride and methylene dianiline; single route, at plant; aromatic polyimide | DE | agg | ts |
Polylactic acid (PLA) fibers extruding, spinning, fiber part processing; single producer, at plant; melting point: 150-160 °C | DE | agg | ts |
Polyphtalamide (PPA) polycondensation of hexamethylene diamine (HMDA) and terephtalic acid (TPA); single route, at plant; estimation | DE | agg | ts |
Polypropylene (PP from Cracker) steam cracker, polymerisation of propene; production mix, at plant; 0.9- 0.915 g/cm3, 42.08 g/mol per repeating unit | JP | agg | ts |
Polypropylene / nitrile butadiene rubber copolymer (PP/NBR, TPE-V) dynamic vulcanisation; single route, at plant; PP/NBR, TPE-V | DE | agg | ts |
Polypropylene / styrene-butadiene rubber copolymer (PP/SBR, TPE-V) (dynamic vulcanisation) dynamic vulcanisation; single route, at plant; PP/SBR, TPE-V | DE | agg | ts |
Polypropylene Film (PP) without additives calendering; single producer, at plant; without additives | US | agg | ts |
Polypropylene granulate (PP) polymerisation of propene; production mix, at plant; 0.91 g/cm3, 42.08 g/mol per repeating unit | EU-28 | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | BE | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | DE | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | EU-28 | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | FR | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | NL | agg | ts |
Polystyrene High Impact Granulate (HI-PS) polymerisation of styrene; production mix, at plant; 1.05 g/cm3, 104.15 g/mol per repeating unit | GB | agg | ts |
Polysulfone (PSU) Polycondensation of bisphenol A sodium salt with 4,4'-Dichlorosulfonyl diphenylmethane; single producer, at plant; PSU | DE | agg | ts |
Polytetramethylen Ether Glycol (via Tetrahydroflourethan) (PTMEG) polymerization of tetrahydrofuran; single route, at plant; 0.982 g/cm3, molar mass per chain unit 73 g/mol | DE | agg | ts |
Polyurethane (PU) semi-rigid (biobased from rapeseed) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; 25.5 MJ/kg net calorific value | EU-28 | p-agg | ts |
Polyurethane (PU, PUR) semi-rigid from rapeseed technology mix, transesterification, epoxidation, polyaddition; production mix, at producer; from rapeseed, semi-rigid | EU-28 | agg | ts |
Polyvinyl acetate (PVAC) (estimation) polymerization of vinylacetate; single producer, at plant; 1170–1200 kg/m3, 86.09 g/mol per repeating unit | DE | agg | ts |
Polyvinyl acetate (PVAC) (estimation) polymerization of vinylacetate; single producer, at plant; 1170–1200 kg/m3, 1170–1200 kg/m3, 86.09 g/mol per repeating unit | EU-28 | agg | ts |
Polyvinyl acetate (PVAC) powder (spray dried) polymerization of vinylacetate, powder via spray drying of PVAC dispersion; single producer, at plant; 86.09 g/mol per repeating unit | DE | agg | ts |
Polyvinyl Alcohol fibers (PVAL) (estimation) Dry spinning, low draft spinning; single route, at plant; PVAL fibers | DE | agg | ts |
Polyvinyl butyral (PVB) (estimation) polymerisation of polyvinyl alcohol; single route, at plant; 142 g/mol per repeating unit | US | agg | ts |
Polyvinyl chloride cable insulation (from S-PVC) polymerisation of vinyl chloride, cable insulation production; production mix, at plant; 62 g/mol per repeating unit | DE | agg | ts |
Polyvinyl chloride fibers (PVC) (estimation from PET) spinning of polyvinyl chloride and epoxy resin; production mix, at plant; 62 g/mol per repeating unit | DE | agg | ts |
Polyvinyl chloride granulate (E-PVC) via acetylene/calcium carbide route (coal based) polymerisation of vinyl chloride via acetylene/calcium carbide route; single route, at plant; 62 g/mol per repeating unit | CN | agg | ts |
Polyvinyl Chloride Granulate (E-PVC), from VCM via ethylene based on 100% natural gas polymerisation of vinyl chloride via ethylene based on 100% natural gas; single route, at plant; 62 g/mol per repeating unit | US | agg | ts |
Polyvinylidenchlorid (PVDC) Film polymerization of vinylidene chloride, extruding and calendering; single producer, at plant; 1.76–1.78 g/cm3, molar mass per chain unit 64.03 g/mol | DE | agg | ts |
Polyvinylidene fluoride (PVDF) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; Net calorific value 16.1 MJ/kg | EU-28 | p-agg | ts |
Poplar (field border) (50% H2O content) Poplar cultivation, harvesting; single route, at field border; 50% water content, 7,7 MJ/kg net calorific value | US | agg | ts |
Pork fat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Pork fat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Potassium carbonate (K2CO3) reaction of potassium hydroxide and carbon dioxide; single route, at plant; 2.43 g/cm3, 138.205 g/mol | EU-28 | agg | ts |
Potassium chloride (agrarian) potassium chloride mining and processing; production mix, at plant; potassium compound content: 60% | EU-28 | agg | ts |
Potassium hydroxide (KOH) via electrolysis of potassium chloride; production mix, at plant; esitmation, 2.04 g/cm3, 56.11 g/mol | DE | agg | ts |
Potassium hydroxide (KOH) (45%) via electrolysis of potassium chloride; production mix, at plant; 45% concentrated | DE | agg | ts |
Potassium hydroxide (KOH) (48%) via electrolysis of potassium chloride; production mix, at plant; 48% concentrated | DE | agg | ts |
Potassium hydroxide (KOH) (50%) via electrolysis of potassium chloride; single route, at plant; estimation, 50% concentrated | DE | agg | ts |
Potassium hydroxide (KOH) (50%) via electrolysis of potassium chloride; production mix, at plant; 50% concentrated | ES | agg | ts |
Potassium hydroxide (KOH) (estimation) via electrolysis of potassium chloride; production mix, at plant; 2.04 g/cm3, 56.11 g/mol | EU-28 | agg | ts |
Potassium iodide (estimation) reaction of potassium hydroxide and iodine, reduction of potassium iodate with coal; production mix, at plant; 3.13 g/cm3, 166.00 g/mol | DE | agg | ts |
Potassium nitrate from potassium chloride and nitric acid (estimation) reaction of potassium chloride and nitric acid; single route, at plant; 2.11 g/cm3, 101.10 g/mol | US | agg | ts |
Poultry by-products for petfood and mechanically separated poultry - no allocation of co-products slaughtering (economic allocation) and processing (no allocation); single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | p-agg | ts |
Poultry by-products for petfood and mechanically separated poultry - no allocation of co-products slaughtering (economic allocation) and processing (no allocation); single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | p-agg | ts |
Poultry by-products for petfood, co-product mechanically separated poultry (mass allocation) slaughtering (economic allocation) and processing (mass allocation); single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Poultry by-products for petfood, co-product mechanically separated poultry (mass allocation) slaughtering (economic allocation) and processing (mass allocation); single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Poultry by-products meal (PBM) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Poultry by-products meal (PBM) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Poultry by-products meal (PBM) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | ZA | agg | ts |
Poultry by-products meal (PBM) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Poultry by-products meal (PBM) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Poultry fat (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Poultry fat (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Poultry meat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Poultry meat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Poultry meat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | ZA | agg | ts |
Poultry meat, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Precious metal recycling recycling of platinum group metals (PGM) from catalytic converter; single route, at plant | DE | p-agg | ts |
Process steam from biomass (solid) 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | NL | p-agg | ts |
Process steam from hard coal 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | KR | agg | ts |
Process steam from hard coal 90% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | KR | agg | ts |
Process steam from hard coal 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | KR | agg | ts |
Process steam from heavy fuel oil (HFO) 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | SA | agg | ts |
Process steam from heavy fuel oil (HFO) 90% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | SA | agg | ts |
Process steam from heavy fuel oil (HFO) 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | SA | agg | ts |
Process steam from light fuel oil (LFO) 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | SA | agg | ts |
Process steam from light fuel oil (LFO) 90% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | SA | agg | ts |
Process steam from light fuel oil (LFO) 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | SA | agg | ts |
Process steam from natural gas 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | KR | agg | ts |
Process steam from natural gas 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | SA | agg | ts |
Process steam from natural gas 85% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 85% efficiency | MX | agg | ts |
Process steam from natural gas 90 % technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | KR | agg | ts |
Process steam from natural gas 90 % technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | SA | agg | ts |
Process steam from natural gas 90% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | MX | agg | ts |
Process steam from natural gas 90% (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | BR | agg | ts |
Process steam from natural gas 90% (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | EU-28 | agg | ts |
Process steam from natural gas 90% (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | CN | agg | ts |
Process steam from natural gas 90% (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | US | agg | ts |
Process steam from natural gas 90% (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | CN | agg | ts |
Process steam from natural gas 90% (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | EU-28 | agg | ts |
Process steam from natural gas 90% (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | US | agg | ts |
Process steam from natural gas 90% (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 90% efficiency | BR | agg | ts |
Process steam from natural gas 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | KR | agg | ts |
Process steam from natural gas 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | SA | agg | ts |
Process steam from natural gas 95% technology mix regarding firing and flue gas cleaning; production mix, at heat plant; MJ, 95% efficiency | MX | agg | ts |
Propane at refinery from crude oil; production mix, at refinery | DE | agg | ts |
Propane at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Propane at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Propane at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Propene (propylene) steam cracker; single route, at plant; 1.91 kg/m3, 42.08 g/mol, | AU | agg | ts |
Propene (propylene) steam cracker; single route, at plant; 1.91 kg/m3, 42.08 g/mol, | ES | agg | ts |
Propene (propylene) steam cracker; single route, at plant; 1.91 kg/m3, 42.08 g/mol, | FR | agg | ts |
Propene (propylene) steam cracker; single route, at plant; 1.91 kg/m3, 42.08 g/mol, | MY | agg | ts |
Propylamine (estimation) produced via isopropanol with ammonia; single route, at producer; 59.11 g/mol, Colorless liquid, 719 kg/m3 | DE | agg | ts |
Propylene at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Propylene at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Propylene at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Propylene carbonate from propylene oxide and carbon dioxide; single route, at plant; 1.21 g/cm3, 102.09 g/mol | DE | agg | ts |
Propylene carbonate from propylene oxide and carbon dioxide; single route, at plant; 1.21 g/cm3, 102.09 g/mol | JP | agg | ts |
Propylene dichloride by-product propylene oxide (Chlorohydrin Process with Ca(OH)2) chlorohydrination, dehydrochlorination, purification; single route, at plant; 1.16 g/cm3, 112.98 g/mol | DE | agg | ts |
Propylene glycol via PO-hydrogenation; single route, at plant; 1.04 g/cm3, 76.10 g/mol | EU-28 | agg | ts |
Propylene glycol monomethyl ether (Methoxypropanol) PGME base- catalyzed reaction of propylene oxide and methanol; single producer, at plant; 0.938 g/cm3, 90.121 g/mol. | US | agg | ts |
Propylene Oxide (Chlorohydrin Process with Cell Liquor) purified, from cell liquor neutralisation; single route, at plant; 0.830 g/cm3, 58 g/mol | EU-28 | agg | ts |
Propylene oxide (Chlorohydrin process) (alloc. mass no credit Calciumhypochlorite) purified, chlorohydrin process, from propene, chlorine and lime; single route, at plant; 0.830 g/cm3, 58 g/mol | DE | agg | ts |
Propylene oxide by-product t-butanol (Oxirane process) (mass allocated) purified, oxirane- process, from isobutane; single route, at plant; 0.83 g/cm3, 58 g/mol | DE | agg | ts |
Propylene Tetramer UOP catalytic condensation process from propylene; single route, at plant; 0.77 g/cm3 | US | agg | ts |
Propylene via ethanol (biobased from BR sugar cane) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | DE | agg | ts |
Propylene via ethanol (biobased from BR sugar cane) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | EU-28 | agg | ts |
Propylene via ethanol (biobased from BR sugar cane) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | US | agg | ts |
Propylene via ethanol (biobased from corn) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | EU-28 | agg | ts |
Propylene via ethanol (biobased from DE wheat) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | EU-28 | agg | ts |
Propylene via ethanol (biobased from DE wheat) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | DE | agg | ts |
Propylene via ethanol (biobased from sugar beet) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | EU-28 | agg | ts |
Propylene via ethanol (biobased from sugar beet) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | DE | agg | ts |
Propylene via ethanol (biobased from US corn) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | US | agg | ts |
Propylene via ethanol (biobased from US corn) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | DE | agg | ts |
Propylene via ethanol (biobased from wheat) biobased ethanol production, dehydration, dimerization, metathesis and isomerization; single route, at plant; 1.81 kg/m3, 42 g/mol, 46 MJ/kg net calorific value | US | agg | ts |
Propylenglycolmonomethylether (Methoxypropanol) PGME base- catalyzed reaction of propylene oxide and methanol; single route, at plant; 0.938 g/cm3, 90.121 g/mol | DE | agg | ts |
PUR dispersion A Polymerization of isocyanate, mixing with water; single producer, at plant; dispersion A | DE | agg | ts |
Purified terephthalic acid (PTA) Amoco process; production mix, at plant; 1.522 g/cm³, 166.13 g/mol | DE | p-agg | ts |
Purified terephthalic acid (PTA) Amoco process; production mix, at plant; 1.522 g/cm³, 166.13 g/mol | IN | agg | ts |
Quartz flour mining, cleaning, grinding, screening; production mix, at plant; 2.65 g/cm3 | DE | agg | ts |
Quartz flour mining, cleaning, grinding, screening; production mix, at plant; 2.65 g/cm3 | EU-28 | agg | ts |
R-1234yf production (estimation) CTFE route; single route, at plant; 1.1 g/cm3, 114 g/mol | DE | agg | ts |
R-1234yf production (estimation, no allocation or credit for co-products) CTFE route, no allocation or credit for any co product from CFC 113 production step; single route, at plant; 1.1 g/cm3, 114 g/mol | DE | p-agg | ts |
Rapeseed meal (wet mill) (economic allocation) Preconditioning, pressing, extraction, refining; single producer, at plant; rapeseed presscake, 53% carbon content | FR | agg | ts |
Rapeseed methylester (RME) price, C mass allocated; production mix, at plant; 78% carbon content, 37 MJ/kg net calorific value, by-product Glycerin | DE | agg | ts |
Rapeseed oil, crude (economic allocation) rape cultivation, rapseed meal and oil production; single producer, at plant; crude oil | EU-28 | agg | ts |
Recycled polyethylene terephthalate (PET) plastic from post-consumer waste, via washing, granulation, pelletization; single route, at producer; 1.38 g/cm3, 192.17 g/mol | US | agg | ts |
Refined palm oil refining of palm oil; single route, at plant; 36.3 MJ/kg net calorific value | DE | agg | ts |
Refinery gas at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Refinery gas at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Refinery gas at refinery from crude oil; production mix, at refinery | MY | agg | ts |
Residual forest wood (cut off approach) incl transport collection of residual forest wood (transport); single route, at producer; 50 km by truck, 400 km by ship | EU-28 | agg | ts |
Rice bran (dry mill) (estimation) paddy rice cultivation and processing of rice grain into white rice; production mix, at plant; Rice bran (13,3% CP) | MY | agg | ts |
Ruthenium mining, transport, separation: mechanical separation, smelting, magnetic separation, chemical refining; production mix, at plant; 12.37 g/cm3, 101.07 g/mol | ZA | agg | ts |
Sebacic Acid by-product 2-Octanol - best case scenario Saponification of castor oil with alkali; single route, at plant; 1.21 g/cm3, 202.25 g/mol | CN | agg | ts |
Sebacic Acid by-product 2-Octanol - worst case scenario Saponification of castor oil with alkali; single route, at plant; 1.21 g/cm3, 202.25 g/mol | CN | agg | ts |
Selenium powder (from copper anode sludge) Direct oxidation (acid roating) of copper anode sludge containing Ag, Au, Se; single route, at plant; 78.97 g/mol | DE | p-agg | ts |
Selenium powder (from copper anode sludge) Direct oxidation/ acid roasting of copper anode sludge containing silver, gold, selenium; single route, at plant; 78.97 g/mol | DE | agg | ts |
Semi-boneless pork, from slaughterhouse (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | EU-28 | agg | ts |
Semicarbazide Hydrochloride from semicarbacide, hydrochloric acid and methanol; single route, at plant; 111.53 g/mol | EU-28 | agg | ts |
Semiconductor manufacturing flash memory 45 nm tech node technology mix; production mix, at plant; flash memory 45 nm tech node | GLO | agg | ts |
Semiconductor manufacturing WLP CSP CMOS logic 14 nm tech node technology mix; production mix, at plant; specification according to the process name | GLO | agg | ts |
Semiconductor manufacturing WLP CSP CMOS logic 22 nm tech node technology mix; production mix, at plant; specification according to the process name | GLO | agg | ts |
Semiconductor manufacturing WLP CSP CMOS logic with on-chip flash memory 130 nm tech node technology mix; production mix, at plant; specification according to the process name | GLO | agg | ts |
Semiconductor manufacturing WLP CSP DRAM 57 nm tech node technology mix; production mix, at plant; specification according to the process name | GLO | agg | ts |
Semiconductor manufacturing WLP CSP flash memory 45 nm tech node technology mix; production mix, at plant; specification according to the process name | GLO | agg | ts |
Silica (pyrogen over silanes) (estimation) pyrogen over silanes; single route, at plant; bulk density 50 –120 g/L | DE | agg | ts |
Silica sand (flour) silica sand grinding; production mix, at plant; grain size in the micrometer range | EU-28 | agg | ts |
Silica sand (flour) silica sand grinding; production mix, at plant; grain size in the micrometer range | CN | agg | ts |
Silicic acid (estimation) acidification of sodium silicate and precipitated; single route, at plant; 96.11 g/mol | DE | agg | ts |
Silicon Nitride Component (hot isostatic press sintering) hot isostatic press sintering; single route, at plant; 3.44 g/cm3, 140.28 g/mol | EU-28 | p-agg | ts |
Silicon Nitride Powder (reaction-bonded) reaction-bonded; single route, at plant; 3.44 g/cm3, 140.28 g/mol | EU-28 | agg | ts |
Silicone fluids (highly viscous) / polydimethylsiloxanes (from organosilanes) from organosilanes; single route, at plant; highly viscous | DE | agg | ts |
Silicone fluids (low viscosity) from organosilane; production mix, at plant; low viscous | EU-28 | agg | ts |
Siloxane (cyclic) (from organosilanes) from organosilanes; single route, at plant; cyclic | DE | agg | ts |
Silver nitrate dissolving silver in hot nitric acid; production mix, at plant; 4.35 g/cm3, 169.87 g/mol | US | agg | ts |
Silver nitrate dissolving silver in hot nitric acid; production mix, at plant; 4.35 g/cm3, 169.87 g/mol | EU-28 | agg | ts |
Silyl terminated prepolymer copolimerization, reaction with silane; single producer, at plant; molar mass of the polymer >4000- 20000g/mol | DE | agg | ts |
Skim milk (fat content) pre-treated, pasteurized, skim milk powder; production mix, at plant; low fat content | US | agg | ts |
Soda (Na2CO3) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | IN | agg | ts |
Soda (Na2CO3) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | JP | agg | ts |
Soda (Na2CO3) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | AU | agg | ts |
Soda (Na2CO3) (estimation) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | CN | agg | ts |
Soda (Na2CO3) (estimation) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | TH | agg | ts |
Soda (Na2CO3) (estimation) Solvay process, from calcium carbonate and sodium chloride; production mix, at plant; 2.53 g/cm3, 105.99 g/mol | MY | agg | ts |
Sodium chlorate (from sodium chloride) electrolysis of sodium chloride; production mix, at factory; 2.54 g/cm3, 106 g/mol | DE | agg | ts |
Sodium chloride (rock salt) mining and processing; production mix, at plant; 2.17 g/cm3, 58.44 g/mol | AU | agg | ts |
Sodium chloride (rock salt) mining and processing; production mix, at plant; 2.17 g/cm3, 58.44 g/mol | JP | agg | ts |
Sodium chloride (rock salt) (estimation) mining and processing; production mix, at plant; 2.165 g/cm3, 58.44 g/mol | IN | agg | ts |
Sodium chloride (rock salt) (estimation) mining and processing; production mix, at plant; 2.17 g/cm3, 58.44 g/mol | RU | agg | ts |
Sodium chloride (rock salt) (estimation) mining and processing; production mix, at plant; 2.165 g/cm3, 58.44 g/mol | TH | agg | ts |
Sodium chloride (rock salt) (estimation) mining and processing; production mix, at plant; 2.165 g/cm3, 58.44 g/mol | CN | agg | ts |
Sodium formate from sodium hydroxide and carbon monoxide; single route, at plant; 1.92 g/cm3, 68.01 g/mol | EU-28 | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | CZ | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | PL | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | RO | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | SE | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | PT | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | JP | agg | ts |
Sodium hydroxide (caustic soda) mix (100%) technology mix; production mix, at plant; 100% | HU | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | JP | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | IT | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | US | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | BE | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | EU-28 | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | ES | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | NL | agg | ts |
Sodium hydroxide mix (50%) technology mix; consumption mix, to consumer; 50% | FR | agg | ts |
Sodium metal (incl. protective oil) Electrolysis of rock salt; single route, at plant; 0.968 g/cm3, 22.99 g/mol | US | agg | ts |
Sodium metal (incl. protective oil) Electrolysis of rock salt; single route, at plant; 0.968 g/cm3, 22.99 g/mol | EU-28 | agg | ts |
Sodium metal (incl. protective oil) Electrolysis of rock salt; single route, at plant; 0.968 g/cm3, 22.99 g/mol | FR | agg | ts |
Sodium metal (incl. protective oil) Electrolysis of rock salt; single route, at plant; 0.968 g/cm3, 22.99 g/mol | DE | agg | ts |
Sodium peroxydisulphate electrolysis of sodium sulphate and sulphuric acid; production mix, at plant; 2.59 g/cm3, 238.10 g/mol | DE | agg | ts |
Sodium peroxydisulphate (estimation) electrolysis of sodium sulphate and sulphuric acid; production mix, at plant; 2.59 g/cm3, 238.10 g/mol | US | agg | ts |
Sodium thiosulfate (estimation) reaction of sulphur and sodium sulfite; single route, at producer | EU-28 | agg | ts |
Solid-Bleached sulfate (SBS) coated on one side (estimation) chemical pulp production, paperboard processing and coating; single route, at plant; coating is 10% of total mass | CN | agg | ts |
Sorghum grains (20% H2O content) (estimation) technology mix; production mix, at field border; 20% H2O | BR | agg | ts |
Sorghum grains cultivation (20% H2O content) summer cultivation; production mix, at field border; 20% H2O content | AU | agg | ts |
Sorghum grains cultivation (20% H2O content) (estimation) technology mix; production mix, at field edge; 20% H2O | DE | agg | ts |
Soy methylester (SME) by-product Glycerine (price, C mas allocated, estimation) by-product glycerine, soy oil production, refining, transesterification; production mix, at plant; 78% total carbon content, 74% biogenic carbon content | BR | agg | ts |
Soy methylester (SME) by-product Glycerine (price, C mass allocated, estimation) by-product glycerine, soy oil production, refining, transesterification; production mix, at plant; 78% total carbon content, 74% biogenic carbon content | EU-28 | agg | ts |
Soy methylester (SME) by-product Glycerine (price, C mass allocated, estimation) by-product glycerine, soy oil production, refining, transesterification; production mix, at plant; 78% total carbon content, 74% biogenic carbon content | US | agg | ts |
Soybean cake (meal from wet mill) (estimation) soybean cultivation and wet mill with solvent extraction; production mix, at plant; Soybean meal hexane extracted (48% crude protein) | IN | agg | ts |
Soybean meal (wet mill) (economic allocation) soybean cultivation and wet mill with pressing and solvent extraction; single producer, at plant; soybean meal hexane extracted (48% CP) | AR | agg | ts |
Soybean meals (from wet mill) (estimation) oil with solvent extraction; production mix, at plant; raw oil | RU | agg | ts |
Soybean oil soybean cultivation and wet mill with pressing and solvent extraction, import from US; single producer, at plant; 77.8% carbon content, 36.6 MJ/kg net calorific value | NZ | agg | ts |
Soybean oil (from wet mill) (estimation) oil with solvent extraction; production mix, at plant; raw oil | RU | agg | ts |
Spring barley grains (14% H2O content; 12% RP) (estimation) spring barley cultivation and harvesting; production mix, at field border; 14% H2O, 12% RP | RU | agg | ts |
Spring barley grains cultivation (14% H2O content; 12% RP) (estimation) Spring barley grain cultivation; production mix, at field border; 14% H2O content | FR | agg | ts |
Stainless steel screw Cold heading, thread rolling; production mix, at plant; stainless steel | EU-28 | p-agg | ts |
Stainless steel sheet (including stamping and bending) stainless steel sheet production (sheet stamping and folding); single producer, at plant; 5% loss (stamping) | DE | agg | ts |
Starch (Polyglucose) corn cultivation, wet milling, drying; single producer, at plant; dried starch | DE | agg | ts |
Starch glue (for paper/cardboard) wet milling, starch extraction; single producer, at plant | DE | agg | ts |
Starch glue (for paper/cardboard) wet milling, starch extraction; single producer, at plant | EU-28 | agg | ts |
Starter fluorescent lamp socket (DfX) technology mix; production mix, at plant; 1 piece | DE | agg | ts |
Stearic acid via hydration of oleic acid from rape oil; production mix, at plant; 0.94 g/cm3, 284.48 g/mol | DE | agg | ts |
Stearic acid via hydration of oleic acid from rape oil; production mix, at plant; 0.94 g/cm3, 284.48 g/mol | EU-28 | agg | ts |
Steel billet (22MnB5) (BOF) blast furnace route; single route, at plant; Crude steel, 22MnB5, alloys: 0.08% Al, 0.30% Cr, 1.40% Mn, 0.40% Si | DE | p-agg | ts |
Steel cold rolled coil (22MnB5) (BOF) blast furnace route; single route, at plant; <1,5mm; 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si | DE | p-agg | ts |
Steel hot rolled coil (22MnB5) (BOF) blast furnace route; single route, at plant; <1,5mm, 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si | DE | p-agg | ts |
Steel screw (hardened and galvanized) steel rolling, hardening, galvanizing; single route, at plant; carbon steel, hardened and galvanized | DE | p-agg | ts |
Steel screw (unalloyed, galvanized) electrogalvanization; single route, at plant; 8.4 kg/m2 | EU-28 | p-agg | ts |
Steel sheet (22MnB5) (BOF) (aluminized, double sides) blast furnace route; single route, at plant; 0,75mm steel thickness - 25 micrometer Aluminized both sides, 22MnB5, alloys: 0,08% Al; 0,30% Cr; 1,40% Mn; 0,40% Si | DE | p-agg | ts |
Stored thermal energy from concentrated solar power Compact linear fresnel reflector (CLFR) concentrated solar power (CSP) technology and molten salt thermal energy storage (TES); single route, at plant; MJ | US | agg | ts |
Styrene acrylate acrylic acid ester production from propene, reaction with styrene; single route, at producer | EU-28 | agg | ts |
Styrene acrylate acrylic acid ester production from propene, reaction with styrene; single route, at producer | DE | agg | ts |
Styrene acrylonitrile (SAN) copolymerization of styrene and acrylonitrile; single route, at plant; 1.09 g/cm3 | DE | agg | ts |
Styrene acrylonitrile (SAN) in waste incineration plant waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; SAN waste | DE | p-agg | ts |
Styrene butadiene block copolymer (SBC, TPE-S) copolymerization of styrene and butadiene; single route, at plant | DE | agg | ts |
Styrene butadiene copolymer (SBC, TPE-S) star block anionic polymerization; production mix, at plant; 70% butadiene, 30% styrene | EU-28 | agg | ts |
Styrene butadiene copolymer (SBS, TPE-S) star block anionic polymerization; production mix, at plant; 70% butadiene, 30% styrene | DE | agg | ts |
Styrene ethene butene styrene copolymer (SEBS, TPE-S) copolymerization (ethylene, butylene, styrene); production mix, at plant; 25 MJ/kg net calorific value | DE | agg | ts |
Styrene ethene propene styrene copolymer (SEPS, TPE-S) polymerization of ethene, propene, styrene...; production mix, at plant; 25 MJ/kg net calorific value | DE | agg | ts |
Styrene isoprene styrene copolymer (SIS, TPE-S) tri block copolymerization (isoprene, styrene); production mix, at plant | DE | agg | ts |
Styrene maleic anhydride copolymer (SMA) copolymerization of styrene and maleic anhydride; production mix, at plant; 1.08 g/cm3 | BE | agg | ts |
Styrene maleic anhydride copolymer (SMA) copolymerization of styrene and maleic anhydride; production mix, at plant; 1.08 g/cm3 | GB | agg | ts |
Styrene maleic anhydride copolymer (SMA) copolymerization of styrene and maleic anhydride; production mix, at plant; 1.08 g/cm3 | DE | agg | ts |
Styrene maleic anhydride copolymer (SMA) copolymerization of styrene and maleic anhydride; production mix, at plant; 1.08 g/cm3 | FR | agg | ts |
Styrene-butadiene rubber (E-SBR, high styrene content 40%) Emulsion polymerization of styrene and butadiene; single producer, at plant; high styrene content 40% | DE | agg | ts |
Styrene-butadiene rubber (E-SBR, low styrene content 23 %) Emulsion polymerization of styrene and butadiene; single producer, at plant; low styrene content 23 % | DE | agg | ts |
Styrene-butadiene rubber (SBR) fiber, fiber production with vulcanisation Emulsion polymerization of styrene and butadiene, vulcanisation and fibration; production mix, at plant; styrene content 27% | DE | agg | ts |
Styrene-butadiene rubber (S-SBR) suspension polymerization of styrene and butadiene; production mix, at plant; 27% styrene content | EU-28 | agg | ts |
Sugar beet pellets, dried (mass allocation) washing, shredding, extraction, drying, pelleting; production mix, at plant; 11% H2O | EU-28 | agg | ts |
Sugar beet syrup sugar juice purification, concentration; single producer, at plant; sirup | EU-28 | agg | ts |
Sugar beet, at field (75% H2O content) Technology mix; Production mix, at field border; 75% water content | EU-28 | agg | ts |
Sugar cane perennial (100% slash and burn) (open press cake and vinasse) Technology mix; production mix, to consumer; 74% H2O; 100% pre-harvest burning | BR | p-agg | ts |
Sugar raw juice (from sugar cane) washing, shredding, extraction, boiling; single producer, at plant | EU-28 | p-agg | ts |
Sugar, at producer (from Brazilian sugar cane) sugarcane cultivation, juice production, sugar refining; single producer, at plant; cane sugar | US | agg | ts |
Sulphur (elemental) at refinery from crude oil; production mix, at refinery; elemental sulphur | RU | agg | ts |
Sulphur (elemental) at refinery from crude oil; production mix, at refinery; elemental sulphur | MY | agg | ts |
Sulphur from natural gas production desulpurisation of natural gas; production mix, at plant; elemental sulphur | NO | agg | ts |
Sulphur from natural gas production desulpurisation of natural gas; production mix, at plant; elemental sulphur | SA | agg | ts |
Sulphur from natural gas production desulpurisation of natural gas; production mix, at plant; elemental sulphur | RU | agg | ts |
Sulphuric acid (37%) oxidation of sulphur; production mix, at plant; 37% concentrated | DE | agg | ts |
Sulphuric acid (75%) oxidation of sulphur; production mix, at plant; 75% concentrated | US | agg | ts |
Sulphuric acid (96%) oxidation of sulphur; production mix, at plant; 96% concentrated | ES | agg | ts |
Sulphuric acid (96%) oxidation of sulphur; production mix, at plant; 96% concentrated | JP | agg | ts |
Sulphuric acid aq. (96%) oxidation of sulphur; production mix, at plant; 96% concentrated | AU | agg | ts |
Sulphuric acid aq. (96%) (estimation) oxidation of sulphur; production mix, at plant; 96% concentrated | CN | agg | ts |
Sulphuric acid aq. (96%) (estimation) oxidation of sulphur; production mix, at plant; 96% concentrated | TH | agg | ts |
Sulphuric acid aq. from natural gas (96%) oxidation of sulphur; production mix, at plant; 96% concentrated | EU-28 | agg | ts |
Sulphuric acid from spent acid plant from used H2SO4 37%; single route, at plant; 96% aqueous solution | EU-28 | p-agg | ts |
Sulphuric acid from spent acid plant from used H2SO4 37%; single route, at plant; 96% aqueous solution | FR | p-agg | ts |
Sulphuric acid mix (96%) technology mix; consumption mix, to consumer; 96% aqueous solution, M= 98.079 g/mol | FR | agg | ts |
Sulphuric acid mix (96%) technology mix; consumption mix, to consumer; 96% aqueous solution, M= 98.079 g/mol | EU-28 | agg | ts |
Sulphuric acid mix (96%) technology mix; consumption mix, to consumer; 96% aqueous solution, M= 98.079 g/mol | ES | agg | ts |
Sun flower (10% H2O content) Sunflower cultivation and harvesting; single route, at field; 10% H2O | FR | agg | ts |
Sunflower oil (estimation) wet mill with solvent extraction; production mix, at plant; 77% carbon content, 25-30% crude protein | DE | agg | ts |
Synthetic graphite mix, average electricity use in graphitization (50% CPC, 50% hard coal coke) from calcined petroleum coke (CPC), from hard coal coke; single route mix, 50% calcined petroleum coke (CPC), 50% hard coal coke, at plant; 2.1- 2.3 g/cm3 | EU-28 | agg | ts |
Synthetic graphite powder (estimate) from hard coal; single route, at plant; 2.1- 2.3 g/cm3 | CN | agg | ts |
Synthetic graphite via calcined petroleum coke, average electricity use in graphitization from petroleum coke; single route, at plant; 2.1- 2.3 g/cm3 | DE | agg | ts |
Synthetic graphite via calcined petroleum coke, average electricity use in graphitization from petroleum coke; single route, at plant; 2.1- 2.3 g/cm3 | US | agg | ts |
Synthetic graphite via calcined petroleum coke, average electricity use in graphitization from petroleum coke; single route, at plant; 2.1- 2.3 g/cm3 | CN | agg | ts |
Synthetic graphite via hard coal coke, average electricity use in graphitization from petroleum coke, from hard coal coke; single route, at plant; 2.1- 2.3 g/cm3 | DE | agg | ts |
Synthetic leather, dry process, incl DMF Synthetic leather, dry process; Single route, at plant; Non-woven textile input 213 g/m2, final product 282 g/m2 | EU-28 | agg | ts |
Synthetic leather, dry process, incl DMF Synthetic leather, dry process; Single route, at plant; Non-woven textile input 213 g/m2, final product 282 g/m2 | US | agg | ts |
Synthetic leather, dry process, incl DMF - open input PE-PP fleece Synthetic leather, dry process; Single route, at plant; Non-woven textile input 213 g/m2, final product 282 g/m2 | US | p-agg | ts |
Synthetic leather, dry process, incl DMF - open input PE-PP fleece Synthetic leather, dry process; Single route, at plant; Non-woven textile input 213 g/m2, final product 282 g/m2 | EU-28 | p-agg | ts |
Synthetic leather, wet + dry process, incl DMF Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 395 g/m2 | US | agg | ts |
Synthetic leather, wet + dry process, incl DMF Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 395 g/m2 | EU-28 | agg | ts |
Synthetic leather, wet + dry process, incl DMF - open input PE-PP fleece Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 395 g/m2 | EU-28 | p-agg | ts |
Synthetic leather, wet + dry process, incl DMF - open input PE-PP fleece Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 395 g/m2 | US | p-agg | ts |
Synthetic leather, wet process, incl DMF Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 326 g/m2 | EU-28 | agg | ts |
Synthetic leather, wet process, incl DMF Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 326 g/m2 | US | agg | ts |
Synthetic leather, wet process, incl DMF - open input PE-PP fleece Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 326 g/m2 | US | p-agg | ts |
Synthetic leather, wet process, incl DMF - open input PE-PP fleece Synthetic leather, wet process; Single route, at plant; Non-woven textile 213g/m2, finished product 326 g/m2 | EU-28 | p-agg | ts |
Talcum (Underground mining, alpine region) technology mix; production mix, at plant; particle size ca.1 micron to 15 microns | EU-28 | agg | ts |
Tall oil (raw product) (2015) (mass allocation) tall oil from kraft paper production, thermal energy sold/used externally; production mix, at plant; 0.32 kg waste paper input per kg tall oil | EU-28 | p-agg | ts/FEFCO |
Tall oil (refinement from paper manufacturing) Dehydration, depitching, fractioning (distillation); production mix, at plant | SE | agg | ts |
Tallow (animal feed) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | BR | agg | ts |
Tallow (animal feed) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | US | agg | ts |
Tallow (animal feed) (economic allocation) slaughtering and processing; single route, at plant; product specification (such as energy, protein and carbon content) given in product flow | NZ | agg | ts |
Tantalum tantalit mining, solvent extraction, tantalum production; production mix, at plant; 16.65 g/cm3, 180.95 g/mol | DE | agg | ts |
Tap water from groundwater filtration, disinfection, ion removement etc.; production mix, at plant; 1000 kg/m3, 18 g/mol | US | agg | ts |
Tap water from groundwater filtration, disinfection, ion removement etc.; production mix, at plant; 1000 kg/m 3,18 g/mol | CN | agg | ts |
Tap water from surface water flockulation, filtration, disinfection, ion removement etc., from surface water; production mix, at plant; 1000 kg/m3, 18 g/mol | DE | agg | ts |
Tap water from surface water flockulation, filtration, disinfection, ion removement etc., from surface water; production mix, at plant; 1000 kg/m3, 18 g/mol | JP | agg | ts |
Tap water from surface water filtration, disinfection, ion removement etc., from surface water; production mix, at plant; 1000 kg/m 3,18 g/mol | CN | agg | ts |
t-butanol by-product propylene oxide Oxirane process; production mix, at plant; 0.79 g/cm3, 74.12 g/mol | DE | agg | ts |
Tellurium production pretreatment, roasting, leaching, electrolysis, purification; production mix, at plant; 6,24 g/cm3, 127.60 g/mol | GLO | p-agg | ts |
Tempered glass 4 mm melting and forming, thermal tempering; production mix, at plant; 2.5 g/cm3, functional unit:10 kg/sqm, thickness: 4 mm | EU-28 | agg | ts |
Terophon (anti drumming compound, Teroson) mixing of water, kaolin, aluminium hydroxide (major components); production mix, at plant | DE | agg | ts |
Tetra isopropyl titanate (stoichiometric) reaction of titanium tetrachloride with isopropanol; production mix, at plant; 0.96 g/cm3, 284.22 g/mol | DE | agg | ts |
Tetra isopropyl titanate (stoichiometric) reaction of titanium tetrachloride with isopropanol; production mix, at plant; 0.96 g/cm3, 284.22 g/mol | EU-28 | agg | ts |
Tetraacetyl ethylenediamine (TAED) reaction of ethylene diamine with acetic acid, reaction of DAED with acetic anhydride; production mix, at plant; 228.25 g/mol | NL | agg | ts |
Tetrachloromethane chlorination of methyl chloride; single route, at plant; 1.48 g/cm3, 119.38 g/mol | DE | agg | ts |
Tetrachlorosilane (silicon tetrachloride) reacting pure silicon with dichloromethane; production mix, at plant; 1.8 g/cm3, 169.90 g/mol | DE | agg | ts |
Tetrafluoroethane (R134a) (estimation) from trichloroethylene and hydrogen fluoride; single route, at plant; 102.03 g/mol | DE | agg | ts |
Tetrafluoroethylene pyrolysis of chlorodifluoromethane; single route, at plant; 1.52 g/cm3, 100.02 g/mol | NL | agg | ts |
Tetrafluoroethylene pyrolysis of chlorodifluoromethane; single route, at plant; 1.52 g/cm3, 100.02 g/mol | IT | agg | ts |
Tetrafluoroethylene pyrolysis of chlorodifluoromethane; single route, at plant; 1.52 g/cm3, 100.02 g/mol | DE | agg | ts |
Tetrafluoroethylene pyrolysis of chlorodifluoromethane; single route, at plant; 1.52 g/cm3, 100.02 g/mol | GB | agg | ts |
Tetrahydrofuran via 1,4-Butanediol via 1,4- Butanediol; single route, at plant; 0.8892 g/cm3, 72.11 g/mol | DE | agg | ts |
Thermal energy and electricity from biomass (solid) - HDF/MDF technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | p-agg | ts |
Thermal energy and electricity from sugar cane bagasse (51% H2O content) combustion of bagasse, CHP plant; single route, at plant; 85% efficiency | GLO | p-agg | ts |
Thermal energy from biomass (solid) - HDF/MDF technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EU-28 | p-agg | ts |
Thermal energy from hard coal technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | MX | agg | ts |
Thermal energy from heavy fuel oil (HFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | SA | agg | ts |
Thermal energy from heavy fuel oil (HFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | CY | agg | ts |
Thermal energy from heavy fuel oil (HFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EE | agg | ts |
Thermal energy from heavy fuel oil (HFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | CZ | agg | ts |
Thermal energy from heavy fuel oil (HFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | BG | agg | ts |
Thermal energy from light fuel oil (LFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | CY | agg | ts |
Thermal energy from light fuel oil (LFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | BG | agg | ts |
Thermal energy from light fuel oil (LFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | CZ | agg | ts |
Thermal energy from light fuel oil (LFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | SA | agg | ts |
Thermal energy from light fuel oil (LFO) technology mix regarding firing and flue gas cleaning; production mix, at heat plant | EE | agg | ts |
Thermal energy from natural gas technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | MX | agg | ts |
Thermal energy from natural gas technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | KR | agg | ts |
Thermal energy from natural gas technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | SA | agg | ts |
Thermal energy from natural gas (CHP) technology mix regarding firing and flue gas cleaning; production mix, at plant | EU-28 | agg | ts |
Thermal energy from natural gas (CHP) (direct) technology mix regarding firing and flue gas cleaning; production mix, at plant | EU-28 | agg | ts |
Thermal energy from natural gas (CHP) (indirect) technology mix regarding firing and flue gas cleaning; production mix, at plant | EU-28 | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | DE | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | DK | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | CH | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NL | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | ES | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NZ | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | GB | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | AU | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | BE | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | EU-28 | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NO | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | IT | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | BR | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | FR | agg | ts |
Thermal energy from natural gas (direct) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | US | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | GB | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NL | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | AU | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | DE | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | FR | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NZ | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | BE | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | US | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | CH | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | NO | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | IT | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | EU-28 | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | BR | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | ES | agg | ts |
Thermal energy from natural gas (indirect) technology mix regarding firing and flue gas cleaning; production mix, at heat plant; 100% efficiency | DK | agg | ts |
Thermal Energy from natural gas 100% technology mix regarding firing and flue gas cleaning; production mix, at heat plant | CN | p-agg | ts |
Thermal energy from natural gas 100% (2011) (domestic production) technology mix regarding firing and flue gas cleaning; single route, at heat plant; 100% efficiency | JP | agg | ts |
Thermoplastic polyurethane (TPU, TPE-U) adhesive reaction of methylene diisocyanate and polyether polyol; production mix, at plant; 66.5% methylene diisocyanate, 33.5% polyether polyol | EU-28 | agg | ts |
Tile and stone cleaner (estimation) material composition; single route, at producer; 75% H2O | DE | agg | ts |
Timber pine saw, lumber; production mix, at plant; 65% moisture | DE | agg | ts |
Tin Bronze (CuSn6) Fire refining and casting, secondary production; single route, at plant; 94% copper, 6% tin | EU-28 | p-agg | ts |
Tin-lead alloy (SnPb37) (estimation) Combining 63% tin and 37% lead; single producer, at plant; SnPb37 | GLO | agg | ts |
Titanium alloy (Ti6Al4V) titanium extraction, processing and alloying; production mix, at plant; 6% aluminium, 4% vanadium | GLO | agg | ts |
Titanium Dioxide Pigment (chloride process) (estimation) chloride process, from rutile; single route, at plant; 4.23 g/cm3, 79.87 g/mol | MY | agg | ts |
Titanium ore extraction and processing ore extraction and processing; production mix, at plant; ilmentite and rutile ores | GLO | agg | ts |
Titanium ore extraction and processing, import DE from AU (ilmenite, sand basis) mining and processing; single route, at plant; 50% TiO2 | DE | agg | ts |
Tomato (97% H2O) tomato cultivation and harvest; production mix, at field border; 97% H2O | CN | agg | ts |
Tribasic lead sulphate (stabilizer, estimation) reaction of lead oxide and a sulfated component; production mix, at plant; 990.86 g/mol | EU-28 | agg | ts |
Tricalcium phosphate Neutralizing slaked lime with phosphoric acid; production mix, at plant; 3.14 g/cm3, 310.18 g/mol | US | agg | ts |
Tricalcium phosphate preparation (estimation) Neutralizing slaked lime with phosphoric acid; production mix, at plant; 3.14 g/cm3, 310.18 g/mol | EU-28 | agg | ts |
Tricresylphosphate (TCP) (estimation) via phosphorous oxychloride and phosphorous acid; production mix, at plant | DE | agg | ts |
Triethylendiamine (TEDA) reaction of ethylene diamine and piperazine; single route, at plant; 112.18 g/mol | EU-28 | agg | ts |
Trimellitic anhydride oxidation of dimethyl benzaldehyde with air; single route, at plant; 192.13 g/mol | DE | agg | ts |
Trimethylamine reaction of methanol and ammonia; production mix, at plant; 670 mg/mL, 59.11 g/mol | DE | agg | ts |
Trimethylolpropane (by-product sodium formate) base- catalyzed reaction of butyraldehyde and formaldehyde, sodium hydroxide used as base, by-product sodium formate; production mix, at plant; density: 1.084 g/mL, molar mass: 134.17 g/mol | CN | agg | ts |
Tripropylene glycol PO-hydrogenation; single route, at plant; 1.02 g/mL, 192.25 g/mol | DE | agg | ts |
Tris (chloro-ethyl) phosphate via ethylene oxide and phosphorus oxychloride; production mix, at plant; 1.39 g/cm3, 285.48 g/mol | DE | agg | ts |
Triticale cultivation (15% H2O content) (estimation) technology mix; production mix, at field border; 15% H2O | DE | agg | ts |
Truck, Euro 4, 12 - 14t gross weight / 9,3t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 12 - 14t gross weight / 9,3t payload capacity | GLO | u-so | ts |
Truck, Euro 4, 14 - 20t gross weight / 11,4t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 14 - 20t gross weight / 11,4t payload capacity | GLO | u-so | ts |
Truck, Euro 4, 20 - 26t gross weight / 17,3t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 20 - 26t gross weight / 17,3t payload capacity | GLO | u-so | ts |
Truck, Euro 4, 26 - 28t gross weight / 18,4t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 26 - 28t gross weight / 18,4t payload capacity | GLO | u-so | ts |
Truck, Euro 4, 28 - 32t gross weight / 22t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 28 - 32t gross weight / 22t payload capacity | GLO | u-so | ts |
Truck, Euro 4, 7,5 t - 12t gross weight / 5t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 7,5 t - 12t gross weight / 5t payload capacity | GLO | u-so | ts |
Truck, Euro 4, more than 32t gross weight / 24,7t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; more than 32t gross weight / 24,7t payload capacity | GLO | u-so | ts |
Truck, Euro 4, up to 7,5t gross weight / 3,3t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; up to 7,5t gross weight / 3,3t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 4, 28 - 34t gross weight / 22t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 28 - 34t gross weight / 22t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 4, 34 - 40t gross weight / 27t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 34 - 40t gross weight / 27t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 4, 50 - 60t gross weight / 40,6t payload capacity diesel driven, Euro 4, cargo; consumption mix; 50 - 60t gross weight / 40,6 t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 4, 50 - 60t gross weight / 40,6t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; 50 - 60t gross weight / 40,6 t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 4, up to 28t gross weight / 12,4t payload capacity (with SCR) diesel driven, Euro 4, cargo; consumption mix; up to 28t gross weight / 12,4t payload capacity | GLO | u-so | ts |
Truck-trailer, Euro 5, 50 - 60t gross weight / 40,6t payload capacity diesel driven, Euro 5, cargo; consumption mix; 50 - 60t gross weight / 40,6t payload capacity | GLO | u-so | ts |
Tungsten Carbide Powder (estimation) reaction of tungsten metal with black carbon; single route, at plant; 15.63 g/cm3, 195.9 g/mol | CN | agg | ts |
Tungsten Metal Powder (estimation) Mining, concentration, pre-treatment, APT production, calcination, tungsten trioxide reduction; single route, at plant; 19,3 g/cm3, 183,8 g/mol | CN | agg | ts |
Turpentine (2015) (mass allocation) turpentine from kraft paper production; single route, at producer; 50% alpha- and beta-pinene content | EU-28 | p-agg | ts/FEFCO |
Tyres (sedan car) mixing, preparation, building, vulcanisation; single route, at producer; around 10 kg weight per tyre | FR | p-agg | ts |
Urea formaldehyde (UF) adhesive system (20% H2O) hydromethylation and condensation reactions of urea and formaldehyde; single route, at plant; 20% H20 | US | agg | ts |
Used passenger car tyre in waste incineration plant (mix) waste-to-energy plant with dry flue gas treatment, without collection, transport and pre-treatment; production mix (region specific plants), at plant; 25.8 MJ/kg net calorific values | EU-28 | p-agg | ts |
Used wood, wood chips (25% H2O content) harvesting, wood chipping; single producer, at plant; 25% water content | GLO | agg | ts |
Used wood, woodchips abs. dry harvesting, wood chipping; single producer, at plant; abs. dry | DE | agg | ts |
Vanadium pentoxide concentrate (V2O5 86%) sodium metavanadate route; production mix, at plant; 3.36 g/cm3, 181.88 g/mol | ZA | agg | ts |
Vat Dye via halogenation of dibenzanthrone; production mix, at plant; 29.9% wt bromine content, 4.1% chlorine content | US | agg | ts |
Vegetable tanning (estimation) vegetable tanning extraction, leather tanning; single route, at plant; tanning extract with 8% moisture content | EU-28 | p-agg | ts |
Vegetable tanning (estimation) vegetable tanning extraction, leather tanning; single route, at plant; tanning extract with 8% moisture content | US | p-agg | ts |
Vinylene carbonate (from ethyl carbonate over hydrochlorination) from ethyl carbonate over hydrochlorination; single route, at plant; 1.36 g/mL, 86.05 g/mol | JP | agg | ts |
Vinylidene dichloride from 1,1,2-trichloroethane; production mix, at plant; 1.21 g/cm3, 96.94 g/mol | DE | agg | ts |
Vinylidene fluoride (1,1-difluoroethylene from chlorodifluoroethane R-142b) dehydrochlorination of chlorodifluoroethane; single route, at plant; 64.03 g/mol | DE | agg | ts |
Washing, average washing of textiles; single operation, at work station; 1 kg of textiles wahed | GLO | u-so | ts |
Water (desalinated; deionised) via ion exchange; single route, at plant; 1000 kg/m3, 18 g/mol | CN | agg | ts |
Water glass (sodium silicate) (solid) reaction of sand with soda ash; single route, at plant; 2.61 g/cm3, 122.06 g/mol | DE | agg | ts |
Water proof agent (C6) and application thick layer (estimation) water proof; single route, at plant; C6, thick layer 2.5 g/m2 | US | p-agg | ts |
Water proof agent (C6) and application thick layer (estimation) water proof; single route, at plant; C6, thick layer 2.5 g/m2 | EU-28 | p-agg | ts |
Water proof agent (C6) and application thin layer (estimation) water repellancy; single route, at plant; C6, thin layer 0.6 g/m2 | EU-28 | p-agg | ts |
Water proof agent (C6) and application thin layer (estimation) water repellancy; single route, at plant; C6, thin layer 0.6 g/m2 | US | p-agg | ts |
Waterglass (sodium silicate) (37/40 solution) mixing of sodium carbonate and quartz sand; single route, at plant; 37/40 solution, silicate water solution | DE | agg | ts |
Wax / Paraffins at refinery from crude oil; production mix, at refinery | RU | agg | ts |
Wax / Paraffins at refinery from crude oil; production mix, at refinery | NL | agg | ts |
Wheat middlings from wheat mill (economic allocation) wheat cultivation, milling and screening; single route, at plant; 16.5% crude protein | US | agg | ts |
Wheel loader (newer standard) diesel- driven wheel loader engine; single operation, at work station; 1 kg diesel combusted | GLO | u-so | ts |
Window glass melting, blowing, drawing, pressing; production mix, at plant; 2500 kg/m3 | DE | agg | ts |
Wine cork (natural) Cork debarking, washing, drying, stamping; single route, at plant; 7% moisture, 50% carbon content | DE | agg | ts |
Winter rape cultivation (75% H2O content) technology mix; production mix, at producer; at field border;75% H2O | DE | agg | ts |
Winter rye grain cultivation (14% H2O content), by-products straw (economic allocation) technology mix; production mix, at field border; 14% H2O | DE | agg | ts |
Winter wheat (15% H2O content) winter wheat cultivation; production mix, at field border; 15% H2O content | AU | agg | ts |
Winter wheat cultivation (grain) (14% H2O content) (estimation) technology mix; production mix, at field border; 14% H2O | CA | agg | ts |
Winter wheat grains (15% H2O content) (estimation) technology mix; production mix, at field border; 15% H2O | CA | agg | ts |
Winter wheat straw cultivation (15% H2O content) technology mix; production mix, at field border; 14% H2O | DE | agg | ts |
Wood pellets (9% H2O content) milling, drying, pelletizing; single producer, at plant; 9% water content | EU-28 | agg | ts |
Wood residue mix milling, drying, pelletizing (depending on kind of wood residue); production mix, at producer (different kinds of residual wood); Wood chips, wood pellets, sawdust, 17% H2O, 14.54 MJ/ kg net calorific value | EU-28 | agg | ts |
Wood soft fibre board chipping and hot pressing; single producer, at plant | DE | agg | ts |
Wooden pallets (EURO, 40% moisture) sawing, piling, nailing; single route, at plant; 40% moisture | EU-28 | agg | ts |
Xylene mix from pyrolysis gasoline; single route, at plant; 0.86- 0.88 g/ml, 106.16 g/mol | DE | agg | ts |
Zinc (remelting) cleaning, melting, refining; single route, at plant; 7.14 g/cm3, 65.38 g/mol | DE | p-agg | ts |
Zinc acetate (anhydrous) (estimation) reaction of zinc metal and acetic acid; production mix, at plant; 183.5 g/mol | EU-28 | agg | ts |
Zinc acetate (anhydrous) (estimation) reaction of zinc metal and acetic acid; production mix, at plant; 183.5 g/mol | DE | agg | ts |
Zinc ammonium chloride (estimation) Acid leaching on metallic zinc with ammonia solution; single route, at producer; white crystalline solid, 243 g/mol | EU-28 | agg | ts |
Zinc cast alloy (GD ZnAl4Cu1) ore mining and beneficiation, two-stage roasting, leaching, electrolysis and re-melting; production mix, at plant; GD ZnAl4Cu1 | DE | agg | ts |
Zinc die casting die casting; single route, at plant; 7.14 g/cm3, 65.38 g/mol | DE | agg | ts |
Zinc mix roasting, leaching, electrowinning; production mix, at plant; 7.14 g/cm3, 65.41 g/mol | GLO | agg | ts |
Zinc oxide (American process) from zinc concentrate/zinc scrap iron, American process; single route, at plant; 5.61 g/cm3, 81.38 g/mol | DE | agg | ts |
Zinc oxide (technology mix: American and French process) technology mix: French process (production from electrolytic zinc) and American process (production from zinc concentrate/ zinc scrap iron); production mix, at plant; 5.61 g/cm3, 81.39 g/mol | GLO | agg | ts |
Zinc oxide high-purity (French process) French process, production from electrolytic zinc; single route, at plant; 5.61 g/cm3, 81.39 g/mol | DE | agg | ts |
Zinc phosphate (estimation) stoichiometric estimation; production mix, at plant; 3.99 g/cm3, 386.11 g/mol | DE | agg | ts |
Zinc powder mining and concentrating, roasting and sintering, leaching, electrolysis, powder production; production mix, at plant; 7.14 g/cm3, 65.38 g/mol | GLO | agg | ts |
Zinc sulphate (ZnSO4) (estimation) reaction of zinc oxide with sulfuric acid; single route, at plant; 161.47 g/mol, 3.54 g/cm3 | DE | agg | ts |
Zircon carbonate (ZrCO3) from zirconium mineral sand; single route, at plant; 431.68 g/mol | GB | agg | ts |