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 |