1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | FR | agg | Sphera |
1,3-Butadiene oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | GB | agg | Sphera |
1,3-Butadiene (Europipeline) oxidative catalytic dehydrogenation of C4 ; production mix, at plant ; 2.4982 kg/m3, 54.09 g/mol | EU-28 | agg | Sphera |
3-Dimethylaminopropylamine (DMAPA) Hydrogenation of 3-(Dimethylamino)propionitril (DMAPN) ; production mix, at producer ; 100% active substance; CAS number: 109-55-7 | EU-28 | agg | Sphera |
Acetone Hock Process, oxidation of cumene ; single route, at plant ; 0.79 g/cm3, 58 g/mol | BE | agg | Sphera |
Acetone Hock Process, oxidation of cumene ; single route, at plant ; 0.79 g/cm3, 58 g/mol | FR | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | GB | agg | Sphera |
Acrylic acid (Propene) oxidation of propene ; production mix, at plant ; 1.05 g/cm3, 72.06 g/mol | FR | agg | Sphera |
Acrylonitrile (AN) ammoxidation of propene ; production mix, at plant ; liquid, density: 0.81 g/cm3, molar mass: 53.06... | GB | agg | Sphera |
Acrylonitrile (AN) ammoxidation of propene ; production mix, at plant ; liquid, density: 0.81 g/cm3, molar mass: 53.06... | DE | agg | Sphera |
Acrylonitrile (AN) ammoxidation of propene ; production mix, at plant ; liquid, density: 0.81 g/cm3, molar mass: 53.06... | IT | agg | Sphera |
Acrylonitrile (AN) ammoxidation of propene ; production mix, at plant ; liquid, density: 0.81 g/cm3, molar mass: 53.06... | NL | agg | Sphera |
Activated carbon technology mix ; production mix, at plant ; porous carbon structure, 35.2 MJ/kg net calori... | DE | agg | Sphera |
Adipic acid oxidation of cyclohexane ; production mix, at plant ; 1.36 g/cm3, 146 g/mol | GB | agg | Sphera |
Adipic acid oxidation of cyclohexane ; production mix, at plant ; 1.36 g/cm3, 146 g/mol | FR | agg | Sphera |
Allyl chloride (C3H5Cl) chlorination of propene ; production mix, at plant ; 0.94 g/cm3, 76.53 g/mol | DE | agg | Sphera |
Allyl chloride (C3H5Cl), by-product hydrochloric acid (100%) chlorination of propene ; production mix, at plant ; 0.94 g/cm3, 76.53 g/mol | EU-28 | agg | Sphera |
Aminoethylethanolamine (AEEA) Production from MEG and Ammonia Hydrogenative amination of monoethylene glycol ; production mix, at producer ; 100% active substance, CAS number: 111-41-1 | EU-28 | agg | Sphera |
Aniline (Phenyl amine, Amino benzene) catalytic hydrogenation of nitrobenzene ; single route, at plant ; 1.022 g/cm3, 93.13 g/mol | FR | agg | Sphera |
Aniline (Phenyl amine, Amino benzene) catalytic hydrogenation of nitrobenzene ; single route, at plant ; 1.022 g/cm3, 93.13 g/mol | BE | agg | Sphera |
Benzene dealkylation of toluene ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | FR | agg | Sphera |
Benzene from pyrolysis fuel ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | IT | agg | Sphera |
Benzene dealkylation of toluene ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | NL | agg | Sphera |
Benzene from pyrolysis fuel ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | FR | agg | Sphera |
Benzene dealkylation of toluene ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | GB | agg | Sphera |
Benzene from pyrolysis fuel ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | GB | agg | Sphera |
Benzene dealkylation of toluene ; production mix, at plant ; 0.88 g/cm3, 78 g/mol, 40.57 MJ/kg net calorifi... | IT | agg | Sphera |
Benzene (from reformate) from reformate ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | GB | agg | Sphera |
Benzene (from reformate) from reformate ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | FR | agg | Sphera |
Benzene (from reformate) from reformate ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | IT | agg | Sphera |
Benzene mix technology mix ; production mix, at plant ; 0.88 g/cm3, 78 g/mol | GB | agg | Sphera |
Bisphenol A technology mix ; production mix, at plant ; solid, density: 1,2 g·cm−3, molar mass: 228,28... | DE | agg | Sphera |
Bisphenol A technology mix ; production mix, at plant ; solid, density: 1,2 g·cm−3, molar mass: 228,28... | NL | agg | Sphera |
Bisphenol A technology mix ; production mix, at plant ; solid, density: 1,2 g·cm−3, molar mass: 228,28... | FR | agg | Sphera |
Butane from C4-raffinate ; production mix, at plant ; gaseous, density: 2,71 g·l−1 (0 °C, 1013 hPa),... | DE | agg | Sphera |
C4 cut (Butadiene) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | NO | agg | Sphera |
C4 cut (Butadiene) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | GB | agg | Sphera |
C4 cut (butadiene) steam cracker ; production mix, at plant ; 45.3 MJ net calorific value | FR | agg | Sphera |
C4 cut (butadiene, Europipeline) technology mix ; production mix, at plant ; 45.3 MJ net calorific value | EU-28 | agg | Sphera |
Caprolactam from Phenol ; production mix, at plant ; solid, density: 1,02 g·cm−3 (75 °C), molar mas... | IT | agg | Sphera |
Caprolactam from Phenol ; production mix, at plant ; solid, density: 1,02 g·cm−3 (75 °C), molar mas... | NL | agg | Sphera |
Carbon dioxide by-product ethylene oxide (EO) via air oxidation of ethylene with air ; single route, at plant ; 1.98 kg/m3, 44.01 g/mol | GB | agg | Sphera |
Carbon dioxide by-product ethylene oxide (EO) via air oxidation of ethylene with air ; single route, at plant ; 1.98 kg/m3, 44.01 g/mol | FR | agg | Sphera |
Chloroacetic acid by catalysed chlorination of acetic acid Catalyzed chlorination of acetic acid ; production mix, at producer ; 100% active substance; CAS number: 79-11-8 | EU-28 | agg | Sphera |
Cumene (C9H12) (based on benzene from reformate) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | CN | agg | Sphera |
Cumene (C9H12) (based on benzene from reformate) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | TH | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | ES | agg | Sphera |
Cumene (isopropylbenzene) (C9H12) alkylation of benzene ; production mix, at plant ; 0.862 g/cm3, 120.20 g/mol | FR | agg | Sphera |
Cyclohexane catalytic hydration of benzene ; production mix, at plant ; 0.7781 g/mL, 84.16 g/mol | NL | agg | Sphera |
Cyclohexane catalytic hydration of benzene ; production mix, at plant ; 0.7781 g/mL, 84.16 g/mol | GB | agg | Sphera |
Dichloromethane chlorination of methyl chloride ; production mix, at plant ; 1.33 g/cm3, 84.93 g/mol | DE | agg | Sphera |
Diethanolamine Reaction of ethylene oxide with excess of ammonia ; production mix, at producer ; 100% active substance, 1.09 g/cm3, 105.14 g... | EU-28 | agg | Sphera |
Di-isononyl phthalate (DINP) esterification of phthalic acid ; production mix, at plant ; 0.98 g/cm3, 418.62 g/mol | DE | agg | Sphera |
Dimethyl carbonate (DMC) liquid phase, from methanol and phosgene, by-product dimethyleneoxalate ; production mix, at plant ; 90.08 g/mol | DE | agg | Sphera |
Dimethyl terephthalate (DMT) oxidation of p-xylene ; production mix, at plant ; 1.35 g/cm3, 194.19 g/mol, 22.8 MJ/kg net calor... | FR | agg | Sphera |
Dimethyl terephthalate (DMT) oxidation of p-xylene ; production mix, at plant ; 1.35 g/cm3, 194.19 g/mol, 22.8 MJ/kg net calor... | NL | agg | Sphera |
Dimethyl terephthalate (DMT) oxidation of p-xylene ; production mix, at plant ; 1.35 g/cm3, 194.19 g/mol, 22.8 MJ/kg net calor... | DE | agg | Sphera |
Dimethyl terephthalate (DMT) oxidation of p-xylene ; production mix, at plant ; 1.35 g/cm3, 194.19 g/mol, 22.8 MJ/kg net calor... | IT | agg | Sphera |
Dimethylamine (Production from Alcohols) reaction of methanol and ammonia ; production mix, at producer ; 0.67 g/cm3, 45.08 g/mol | EU-28 | agg | Sphera |
Dimethylsulphate (DMS) Production via Ethers and SulphurTrioxide Production from ethers and sulphur trioxide ; production mix, at producer ; 100% active substance; CAS number: 77-78-1 | EU-28 | agg | Sphera |
Dinitro toluene nitration of toluene ; production mix, at plant ; solid, molar mass: 182,14 g·mol−1 | IT | agg | Sphera |
Dinitro toluene nitration of toluene ; production mix, at plant ; solid, molar mass: 182,14 g·mol−1 | GB | agg | Sphera |
Dinitro toluene nitration of toluene ; production mix, at plant ; solid, molar mass: 182,14 g·mol−1 | FR | agg | Sphera |
Dinitro toluene nitration of toluene ; production mix, at plant ; solid, molar mass: 182,14 g·mol−1 | DE | agg | Sphera |
Dioctyltin oxide (approximation) hydrolysis of Dialkyltin halide ; production mix, at producer ; 361 g/mol | EU-28 | agg | Sphera |
Epichlorohydrin via allyl chloride ; production mix, at plant ; liquid, density: 1,18 g·cm−3 (20 °C), molar ma... | DE | agg | Sphera |
Ethanol hydrogenation with nitric acid ; single route, at plant ; 96 % concentrated | GB | agg | Sphera |
Ethanol hydrogenation with nitric acid ; single route, at plant ; 96 % concentrated | FR | agg | Sphera |
Ethene (ethylene) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | ES | agg | Sphera |
Ethene (ethylene) steam cracker ; production mix, at plant ; 1.178 kg/m3, 28.05 g/mol | FR | agg | Sphera |
Ethyl benzene liquid phase alkylation ; production mix, at plant ; liquid, density: 0,87 g·cm−3, molar mass: 106,... | NL | agg | Sphera |
Ethyl benzene liquid phase alkylation ; production mix, at plant ; 0.87 g/cm3, 106.17 g/mol | DE | agg | Sphera |
Ethylamine from ethanol and ammonia, by-product Diethylamine, Triethylamine (TEA) ; production mix, at plant ; gaseous, density: 2,162 g·m−3(0 °C, 1013 mbar)... | DE | agg | Sphera |
Ethylene glycol from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | FR | agg | Sphera |
Ethylene glycol from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | GB | agg | Sphera |
Ethylene glycol from ethene and oxygen via ethylene oxide ; production mix, at plant ; 1.11 g/cm³, 62 g/mol | BE | agg | Sphera |
Ethylene oxide (EO) via air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | BE | agg | Sphera |
Ethylene oxide (EO) via air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | NL | agg | Sphera |
Ethylene oxide (EO) via air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | FR | agg | Sphera |
Ethylene oxide (EO) via air oxidation of ethylene with air ; production mix, at plant ; 1.93 kg/m3, 44.05 g/mol | GB | agg | Sphera |
Ethylene oxide (EO) via O2/methane oxidation of ethylene with oxygen ; production mix, at plant ; gaseous, density: 1,93 kg·m−3 (15 °C, 1000 hPa... | DE | agg | Sphera |
Ethylenediaminetetraacetic acid (EDTA) (approximation) Cyanomethylation of ethylene diamine ; single route, at plant ; 0.86 g/cm3, 292.24 g/mol | EU-28 | agg | Sphera |
Ethyne (acetylene) Sachsse-Bartholome process ; production mix, at plant ; 1.18 g/l, 26.04 g/mol | GB | agg | Sphera |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | IT | agg | Sphera |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | NL | agg | Sphera |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | GB | agg | Sphera |
Formaldehyde (HCHO; 37%) dehydrogenation of methanol ; production mix, at plant ; 37 % concentrated | FR | agg | Sphera |
Formic acid (methane acid, 85%) from methanol ; production mix, at plant ; liquid, density: 1.220 g/mL, molar mass: 46.03... | DE | agg | Sphera |
Glycerine (from Epichlorohydrine) via epichlorohydrine ; production mix, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine (refined) by-product rapeseed methyl ester (RME) (energy allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | EU-28 | agg | Sphera |
Glycerine (refined) by-product rapeseed methyl ester (RME) (energy allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine (refined) by-product rapeseed methyl ester (RME) (price 2014 allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine (refined) by-product rapeseed methyl ester (RME) (price 2014 allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | EU-28 | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (energy allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (energy allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | EU-28 | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (price 2014 allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | DE | agg | Sphera |
Glycerine by-product rapeseed methyl ester (RME) (price 2014 allocated) extraction, refining, transesterification ; single route, at plant ; 1.26 g/cm3, 92.09 g/mol | EU-28 | agg | Sphera |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine ; single route, at plant ; 643.71 g/mol | DE | agg | Sphera |
Hexabromododecane (HBCD, 1,2,5,6,9,10-Hexabromododecane) reaction of cyclododecatriene and bromine ; single route, at plant ; 643.71 g/mol | EU-28 | agg | Sphera |
Hexamethylenediamine (HMDA; from acrylonitrile via adiponitrile) HMDA via hydrogenation of adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | JP | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene via adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | DE | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene via adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | US | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene via adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | GB | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) HMDA via hydrogenation of adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | FR | agg | Sphera |
Hexamethylenediamine (HMDA; from butadiene via adiponitrile) from butadiene via adiponitrile ; single route, at plant ; 0.84 g/mL, 116.20 g/mol | FR | agg | Sphera |
Isobutane (from n-butane) via n-butane ; production mix, at plant ; gaseous, density: 2,71 g·l−1 (0 °C, 1013 hPa),... | DE | agg | Sphera |
Isononanoic acid aldehyde oxidation ; production mix, at plant ; liquid, density: 0.897 - 0.903 g/cm3, molar ma... | DE | agg | Sphera |
Isononanol single route ; production mix, at plant ; liquid, density: 0,82 g·cm−3, molar mass: 144.... | DE | agg | Sphera |
Isopropanol indirect hydrogenation ; single route, at plant ; 0.78 g/cm3, 60.10 g·/mol | IT | agg | Sphera |
Isopropanol indirect hydrogenation ; single route, at plant ; 0.78 g/cm3, 60.10 g·/mol | NL | agg | Sphera |
Isopropanol indirect hydrogenation ; single route, at plant ; 0.78 g/cm3, 60.10 g·/mol | FR | agg | Sphera |
Isopropanol indirect hydrogenation ; production mix, at plant ; 0.78 g/cm3, 60.10 g·/mol | GB | agg | Sphera |
Maleic anhydride via oxidation of xylene ; production mix, at plant ; solid, density: 1.48 g/cm3, molar mass: 98.06 ... | DE | agg | Sphera |
Maleic anhydride from n-butane ; production mix, at plant ; solid, density: 1.48 g/cm3, molar mass: 98.06 ... | GB | agg | Sphera |
Maleic anhydride from benzene ; production mix, at plant ; solid, density: 1.48 g/cm3, molar mass: 98.06 ... | IT | agg | Sphera |
Maleic anhydride from n-butane ; production mix, at plant ; solid, density: 1.48 g/cm3, molar mass: 98.06 ... | IT | agg | Sphera |
Maleic anhydride from n-butane ; production mix, at plant ; solid, density: 1.48 g/cm3, molar mass: 98.06 ... | BE | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | ES | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | FR | agg | Sphera |
Methane natural gas purification ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | CN | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | NO | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | IT | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | BE | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | NL | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | EU-28 | agg | Sphera |
Methane purification of natural gas ; single route, at plant ; 0.72 kg/m3, 16.04 g/mol, 50.04 MJ/kg net calorif... | GB | agg | Sphera |
Methanol from natural gas (integrated technologies) from natural gas, integrated technology ; production mix, at plant ; 0.79 g/cm3, 32.04 g/mol | DE | agg | Sphera |
Methanol mix technology mix ; consumption mix, to consumer ; 0.79 g/cm3, 32.04 g/mol | EU-28 | agg | Sphera |
Methyl acetate esterification of methanol with acetic acid ; single route, at plant ; 0.93 g/cm3, 74.08 g/mol | DE | agg | Sphera |
Methyl bromide by-product tetrabromo bisphenol A ; production mix, at plant ; gaseous, density: 3,97 kg·m−3 (0 °C, 1013 hPa)... | DE | agg | Sphera |
Methyl isobutyl ketone (MIBK) from acetone and hydrogen ; production mix, at plant ; 0.80 g/mL, 100 g/mol | DE | agg | Sphera |
Methylene diphenyl diisocyanate (MDI), by-product hydrochloric acid, methanol phosgenation of methylenedianiline ; production mix, at plant ; solid, density: 1,18 g·cm−3, molar mass: 250,2... | BE | agg | Sphera |
Methylene diphenyl diisocyanate (MDI), by-product hydrochloric acid, methanol phosgenation of methylenedianiline ; production mix, at plant ; solid, density: 1,18 g·cm−3, molar mass: 250,2... | FR | agg | Sphera |
Methylmethacrylate (MMA, recycling of spent acid) recycling of spent acid ; production mix, at plant ; 0.94 g/cm³, 100.12 g/mol | GB | agg | Sphera |
Methylmethacrylate (MMA, recycling of spent acid) recycling of spent acid ; production mix, at plant ; 0.94 g/cm³, 100.12 g/mol | FR | agg | Sphera |
Methylmethacrylate (MMA, recycling of spent acid) recycling of spent acid ; production mix, at plant ; 0.94 g/cm³, 100.12 g/mol | NL | agg | Sphera |
N,N-Dimethylaminopropyl Acrylamide (DiMAPA), credit butanol Continuous aminolysis ; production mix, at producer ; 156.229 g/mol | EU-28 | agg | Sphera |
Nitrobenzene from benzene via nitration ; production mix, at plant ; 1.199 g/cm3, 123.06 g/mol | BE | agg | Sphera |
Nitrobenzene from benzene via nitration ; production mix, at plant ; 1.199 g/cm3, 123.06 g/mol | FR | agg | Sphera |
n-Methylpyrolidone (NMP, Butyrolactone via Maleic anhydride) via maleic anhydride ; production mix, at plant ; 1.03 g/cm3, 99 g/mol | DE | agg | Sphera |
Nylon salt 63% solution, AH salt (HMDA from acrylonitrile) HMDA from acrylonitrile ; production mix, at plant ; 63 % concentrated | DE | agg | Sphera |
Nylon salt 63% solution, AH salt (HMDA from butadiene) HMDA from adipic acid ; production mix, at plant ; 63 % concentrated | GB | agg | Sphera |
o-Xylene from pyrolysis gasoline ; single route, at plant ; 0.88 g/ml, 106.17 g/mol | IT | agg | Sphera |
o-Xylene from pyrolysis gasoline ; single route, at plant ; 0.88 g/ml, 106.17 g/mol | FR | agg | Sphera |
o-Xylene from pyrolysis gasoline ; single route, at plant ; 0.88 g/ml, 106.17 g/mol | NL | agg | Sphera |
Phenol Hock Process, oxidation of cumene ; single route, at plant ; 1.07 g/cm3, 94 g/mol | FR | agg | Sphera |
Phenol Hock Process, oxidation of cumene ; single route, at plant ; 1.07 g/cm3, 94 g/mol | BE | agg | Sphera |
Phthalic anhydride via oxidation of xylene ; production mix, at plant ; 1.53 g/cm, 148.12 g/mol | IT | agg | Sphera |
Phthalic anhydride via oxidation of xylene ; production mix, at plant ; 1.53 g/cm, 148.12 g/mol | DE | agg | Sphera |
Phthalic anhydride via oxidation of xylene ; production mix, at plant ; 1.53 g/cm, 148.12 g/mol | NL | agg | Sphera |
Phthalic anhydride via oxidation of xylene ; production mix, at plant ; 1.53 g/cm, 148.12 g/mol | GB | agg | Sphera |
Phthalic anhydride via oxidation of xylene ; production mix, at plant ; 1.53 g/cm, 148.12 g/mol | FR | agg | Sphera |
Production 3-(Dimethylamino)propionitril (DMAPN) - open input dimethylamine Reaction of Dimethyl amine and acrylonitrile ; production mix, at producer ; 0.86 g/cm3, 98.15 g/mol | EU-28 | p-agg | Sphera |
Production dimethyl ether from methanol Catalytic dehydration of methanol ; production mix, at plant ; 2.1146 kg/m3, 46.07 g/mol | EU-28 | agg | Sphera |
Propene (propylene) steam cracker ; single route, at plant ; 1.91 kg/m3, 42.08 g/mol,45.77 MJ/kg net calorifi... | AU | agg | Sphera |
Propene (propylene) steam cracker ; single route, at plant ; 1.91 kg/m3, 42.08 g/mol,45.77 MJ/kg net calorifi... | FR | agg | Sphera |
Propene (propylene) steam cracker ; single route, at plant ; 1.91 kg/m3, 42.08 g/mol,45.77 MJ/kg net calorifi... | ES | agg | Sphera |
Propene (propylene) steam cracker ; single route, at plant ; 1.91 kg/m3, 42.08 g/mol,45.77 MJ/kg net calorifi... | GB | agg | Sphera |
Propylene glycol via PO-hydrogenation ; single route, at plant ; 1.04 g/cm3, 76.10 g/mol | FR | agg | Sphera |
p-Xylene (from reformate) catalytic reforming of petroleum naphtha ; production mix, at plant ; 0.861 g/mL, 106 g/mol | FR | agg | Sphera |
p-Xylene (from reformate) catalytic reforming of petroleum naphtha ; production mix, at plant ; 0.861 g/mL, 106 g/mol | GB | agg | Sphera |
p-Xylene (from reformate) catalytic reforming of petroleum naphtha ; production mix, at plant ; 0.861 g/mL, 106 g/mol | IT | agg | Sphera |
p-Xylene (from reformate) catalytic reforming of petroleum naphtha ; production mix, at plant ; 0.861 g/mL, 106 g/mol | DE | agg | Sphera |
Sodium citrate neutralization of citric acid with sodium hydroxide ; single route, at plant ; 1.7 g/cm3, 258.06 g/mol | DE | agg | Sphera |
Soot (C carrier, from ethyne production) via SACHSSE-BARTHOLOME process ; production mix, at plant ; solid powder | DE | agg | Sphera |
Styrene catalytic dehydrogenation of ethylbenzene (EBSM) ; single route, at plant ; C8H8, CAS 100-42-5, phenylethene | IT | agg | Sphera |
Styrene catalytic dehydrogenation of ethylbenzene (EBSM) ; single route, at plant ; 0.91 g/cm3, 104 g/mol | FR | agg | Sphera |
Styrene catalytic dehydrogenation of ethylbenzene (EBSM) ; single route, at plant ; C8H8, CAS 100-42-5, phenylethene | GB | agg | Sphera |
Styrene catalytic dehydrogenation of ethylbenzene (EBSM) ; single route, at plant ; 0.91 g/cm3, 104 g/mol | BE | agg | Sphera |
Tallow fatty acid (C16-C18 fatty acid from tallow) Hydrolysis and fractionated distillation ; single route, at plant ; CAS 61790-37-2 | EU-28 | agg | Sphera |
Titanium isopropoxide (approximation) reaction of titanium tetrachloride and isopropanol ; production mix, at producer ; 0.96 g/cm3, 284 g/mol | EU-28 | agg | Sphera |
Toluene (from pyrolysis gasoline) from pyrolysis gasoline ; single route, at plant ; 0.87 g/cm3, 92.14 g/mol | NL | agg | Sphera |
Toluene (from pyrolysis gasoline) from pyrolysis gasoline ; production mix, at plant ; 0.87 g/cm3, 92.14 g/mol | IT | agg | Sphera |
Toluene by-product BTX (from reformate) BTX; from reformate ; single route, at plant ; 0.87 g/cm3, 92.14 g/mol | GB | agg | Sphera |
Toluene by-product BTX (from reformate) BTX; from reformate ; single route, at plant ; 0.87 g/cm3, 92.14 g/mol | EU-28 | agg | Sphera |
Toluene by-product BTX (from reformate) BTX; from reformate ; single route, at plant ; 0.87 g/cm3, 92.14 g/mol | FR | agg | Sphera |
Toluene diisocyanate (TDI; Phosgenation) phosgenation of toluenediamine, from carbon monoxide, chlorine, hydrogen and dinitrotoluene ; production mix, at plant ; 1.21 g/cm3, 174.2 g/mol | GB | agg | Sphera |
Toluene diisocyanate (TDI; Phosgenation) phosgenation of toluenediamine ; production mix, at plant ; 1.21 g/cm3, 174.2 g/mol | FR | agg | Sphera |
Triethanolamine (TEA) from ethylene oxide ; production mix, at plant ; 1.12 g/mL, 149.19 g/mol | EU-28 | agg | Sphera |
Urea (stamicarbon process) stami carbon process, from ammonia and carbon dioxide ; production mix, at plant ; 1.32 g/cm3, 60 g/mol | DE | agg | Sphera |
Vinylchloride monomer (VCM) chlorination of ethylene ; production mix, at plant ; 2.86 kg/m3, 62.5 g/mol | GB | agg | Sphera |
Vinylchloride monomer (VCM) chlorination of ethylene ; production mix, at plant ; 2.86 kg/m3, 62.5 g/mol | FR | agg | Sphera |