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 |
