Aluminium hydroxide from aluminium sulphate
based on stoichiometry ;
single route, at plant ;
2.42 g/cm3, 78.00 g/mol | DE | agg | Sphera |
Aluminium Hydroxide from Bauxite
Bayer process, from bauxite ;
consumption mix, at plant ;
2.42 g/cm3, 78.00 g/mol | DE | agg | Sphera |
Ammonia (NH3) production mix, 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 | EU-28 | agg | Sphera |
Ammonia (NH3) synthesis with CO2 recovery, by-product carbon dioxide (without allocation)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | GB | p-agg | Sphera |
Ammonia (NH3) with CO2 recovery, by-product carbon dioxide (economic allocation)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | GB | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | FR | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | IT | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | GB | agg | Sphera |
Ammonia (NH3) without CO2 recovery (carbon dioxide emissions to air)
Haber-Bosch process, from natural gas ;
production mix, at plant ;
0.7714 kg/m3, 17.03 g/mol | NO | agg | Sphera |
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 | Sphera |
Ammonium chloride (Salmiac, Solvay-process)
Solvay process ;
production mix, at plant ;
solid, density: 1,53 g·cm−3, molar mass: 53,49... | DE | agg | Sphera |
Ammonium nitrate
neutralisation of nitric acid wit ammonia ;
production mix, at plant ;
1.73 g/cm3, 80.04 g/mol | EU-28 | agg | Sphera |
Ammonium sulphate mix (by-product)
propene ammoxidation ;
production mix, at plant ;
solid, density: 1,77 g·cm−3, molar mass: 132,1... | DE | agg | Sphera |
Calcium hypochlorite
from sodium chloride production ;
production mix, at plant ;
solid, density: 2,35 g·cm−3, molar mass: 142,9... | DE | 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 | BE | agg | Sphera |
Carbon monoxide via synthesis gas (by-product hydrogen)
cryogenic separation ;
production mix, at plant ;
density: 1,25 kg·m−3 (0 °C, 1013 mbar), molar ... | FR | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (diaphragm)
chlorine alkali electrolysis, diaphragm ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | FR | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | GB | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | BR | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | FR | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | BE | agg | Sphera |
Chlorine from chlorine-alkali-electrolysis (membrane)
chlorine alkali electrolysis, membrane ;
single route, at plant ;
3.2 g/l, 70.9 g/mol | IT | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | BE | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | ES | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | NL | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | NO | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | GB | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | FR | agg | Sphera |
Chlorine mix
technology mix ;
production mix, at plant ;
3.2 kg/m3, 70.9 g/mol | IT | agg | Sphera |
Hydrogen (steam cracker)
steam cracker, from natural gas ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:... | NO | agg | Sphera |
Hydrogen (steam cracker)
steam cracker, from naphtha ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:... | IT | agg | Sphera |
Hydrogen (steam cracker)
steam cracker, from naphtha ;
production mix, at plant ;
gaseous, density: 0,0899 kg · m−3, molar mass:... | GB | agg | Sphera |
Hydrogen (steam reforming heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | EU-28 | agg | Sphera |
Hydrogen (steam reforming heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | GB | agg | Sphera |
Hydrogen (steam reforming heavy fuel oil)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | FR | agg | Sphera |
Hydrogen (steam reforming natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | EU-28 | agg | Sphera |
Hydrogen (steam reforming natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | GB | agg | Sphera |
Hydrogen (steam reforming natural gas)
Steam reforming - heavy fuel oil ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | IT | agg | Sphera |
Hydrogen (steam reforming natural gas)
Steam reforming - natural gas ;
production mix, at plant ;
0.0899 kg/m3, 2 g/cm3 | FR | agg | Sphera |
Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol | GB | agg | Sphera |
Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol | FR | agg | Sphera |
Hydrogen cyanide (prussic acid)
technology mix ;
production mix, at plant ;
0.687 g/cm3, 27.03 g/mol | BE | agg | Sphera |
Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60% | NL | agg | Sphera |
Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60% | IT | agg | Sphera |
Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60% | NO | agg | Sphera |
Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60% | GB | agg | Sphera |
Nitric acid (60%)
oxidation of ammonia ;
single route, at plant ;
60% | FR | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | PL | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | GB | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | CZ | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | HU | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | IT | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | AT | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | ES | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | AU | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | FR | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | SE | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | TH | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | RO | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | NO | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | CH | agg | Sphera |
Nitrogen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.250 kg/m3, 14.0 g/mol | BE | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | TH | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | IT | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | BE | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | GB | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | AU | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | ES | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | NO | agg | Sphera |
Nitrogen (liquid)
via cryogenic air separation ;
production mix, at plant ;
14.0 g/mol | FR | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | TW | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | FR | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | JP | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | ES | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | BE | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | IT | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | NO | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | CA | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | AU | agg | Sphera |
Oxygen (gaseous)
via cryogenic air separation ;
production mix, at plant ;
1.429 kg/m3, 16.0 g/mol | GB | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | BE | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | FR | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | IT | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | SE | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | ES | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | GB | agg | Sphera |
Oxygen (liquid)
via cryogenic air separation ;
production mix, at plant ;
16.0 g/mol | NO | agg | Sphera |
Phosphoric acid (100%) (wet process)
wet process, from raw phosphate and sulphuric acid ;
production mix, at plant ;
100% | EU-28 | agg | Sphera |
Phosphoric acid (100%) (wet process)
wet process, from raw phosphate and sulphuric acid ;
production mix, at plant ;
100% | DE | agg | Sphera |
Phosphoric acid (75%)
wet process ;
production mix, at plant ;
75% | DE | agg | Sphera |
Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride ;
production mix, at plant ;
2.53 g/cm3, 105.99 g/mol | AU | agg | Sphera |
Soda (Na2CO3)
Solvay process, from calcium carbonate and sodium chloride ;
production mix, at plant ;
2.53 g/cm3, 105.99 g/mol | JP | agg | Sphera |
Sodium chloride (rock salt)
mining and processing ;
production mix, at plant ;
2.17 g/cm3, 58.44 g/mol | AU | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | NL | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | RO | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | CZ | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | NO | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | HU | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | ES | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | FR | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | SE | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | PL | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | IT | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | JP | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | PT | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | GB | agg | Sphera |
Sodium hydroxide (caustic soda) mix (100%)
technology mix ;
production mix, at plant ;
100% | BE | agg | Sphera |
Sodium hydroxide from chlorine-alkali-electrolysis (membrane)
from chlorine-alkali electrolysis (membrane), from sodium chloride ;
single route, at plant ;
39.99 g/mol | BR | agg | Sphera |
Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50% | IT | agg | Sphera |
Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50% | BE | agg | Sphera |
Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50% | JP | agg | Sphera |
Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50% | ES | agg | Sphera |
Sodium hydroxide mix (50%)
technology mix ;
consumption mix, to consumer ;
50% | FR | agg | Sphera |
Sulphur (elemental) at refinery
from crude oil ;
production mix, at refinery ;
elemental sulphur | NL | agg | Sphera |
Sulphur (elemental) at refinery
from crude oil ;
production mix, at refinery ;
elemental sulphur | GB | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | GB | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | AU | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | JP | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | ES | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | FR | agg | Sphera |
Sulphuric acid (96%)
oxidation of sulphur ;
production mix, at plant ;
96% concentrated | BE | agg | Sphera |
Sulphuric acid mix (96%) (consumption mix)
technology mix ;
consumption mix, to consumer ;
96% aqueous solution, M= 98.079 g/mol | ES | agg | Sphera |
Sulphuric acid mix (96%) (consumption mix)
technology mix ;
consumption mix, to consumer ;
96% aqueous solution, M= 98.079 g/mol | FR | agg | Sphera |
Titanium dioxide pigment (chloride process)
chloride process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol | DE | agg | Sphera |
Titanium dioxide pigment (chloride process)
chloride process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol | EU-28 | agg | Sphera |
Titanium dioxide pigment (sulphate process)
sulphate process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol | DE | agg | Sphera |
Titanium dioxide pigment (sulphate process)
sulphate process, from rutile ;
single route, at plant ;
4.23 g/cm3, 79.87 g/mol | EU-28 | agg | Sphera |
Trichlorosilane by-product chlorosilanes
Rochow- Müller- Synthesis ;
production mix, at plant ;
1.34 g/cm3, 135.45 g/mol | DE | agg | Sphera |
Trichlorosilane by-product chlorosilanes
Rochow- Müller- Synthesis ;
production mix, at plant ;
1.34 g/cm3, 135.45 g/mol | EU-28 | agg | Sphera |
