Process graph

Chemicals flow into processes and out again. Where one process makes what another uses, the two are linked: that is how value chains, and later linked life-cycle inventories, appear.

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All links as a list (511)

2-Ethylanthraquinone → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Feedstock)
Acetic acid → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Feedstock)
Acetic acid → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Air → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Feedstock)
Air → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Reactant)
Air → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Feedstock)
Air → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Air → Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Feedstock)
Air → Cryogenic air separation unit (500 t/d GOX) (Feedstock)
Air → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Feedstock)
Air → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Feedstock)
Air → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Feedstock)
Air → Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) (Feedstock)
Air → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Feedstock)
Air → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Air → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Air → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Feedstock)
Air → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Feedstock)
Air → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Feedstock)
Air → Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) (Feedstock)
Air → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Air → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Feedstock)
Air → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Feedstock)
Air → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Feedstock)
Air → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Feedstock)
Air → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Feedstock)
Air → Flaring of methane-rich waste gas (Feedstock)
Air → Instrument air, dried, 8 bar(a) (Feedstock)
Air → Steam generation, natural-gas boiler, saturated 11 bar(a) (Feedstock)
Aluminium oxide → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Feedstock)
Ammonia → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Feedstock)
Ammonia → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Ammonia → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Ammonia → Methylamines (MMA, DMA, TMA) from methanol and ammonia (Feedstock)
Ammonia → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Feedstock)
Ammonia → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Ammonia → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Feedstock)
Ammonia → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Feedstock)
Ammonia → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Feedstock)
Bauxite → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Benzene → Cumene by zeolite alkylation of benzene with propylene (Feedstock)
Benzene → Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene (Feedstock)
Bromine → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Feedstock)
Bromine → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Feedstock)
Butane-1,4-diol → Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) (Feedstock)
Butanone (methyl ethyl ketone) → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Calcium hydroxide → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Feedstock)
Calcium hydroxide → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Feedstock)
Calcium oxide → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Calcium oxide → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Carbon dioxide → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Feedstock)
Carbon dioxide → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Feedstock)
Carbon monoxide → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Feedstock)
Carbon monoxide → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Feedstock)
Carbon monoxide → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Feedstock)
Carbon monoxide → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Feedstock)
Carbon monoxide → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Feedstock)
Chilled water → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Utility)
Chilled water → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Utility)
Chilled water → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Utility)
Chilled water → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Utility)
Chilled water → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Utility)
Chlorine → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Feedstock)
Chlorine → Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) (Feedstock)
Chlorine → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Feedstock)
Chlorine → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Feedstock)
Chlorine → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Feedstock)
Chlorine → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Feedstock)
Chlorine dioxide → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Cooling water → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Utility)
Cooling water → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Utility)
Cooling water → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Utility)
Cooling water → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Utility)
Cooling water → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Utility)
Cooling water → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Utility)
Cooling water → Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Utility)
Cooling water → Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) (Utility)
Cooling water → Cryogenic air separation unit (500 t/d GOX) (Utility)
Cooling water → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Utility)
Cooling water → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Utility)
Cooling water → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Utility)
Cooling water → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Utility)
Cooling water → Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) (Utility)
Cooling water → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Utility)
Cooling water → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Utility)
Cooling water → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Utility)
Cooling water → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Utility)
Cooling water → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Utility)
Cooling water → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Utility)
Cooling water → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Utility)
Cooling water → Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) (Utility)
Cooling water → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Utility)
Cooling water → Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) (Utility)
Cooling water → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Utility)
Cooling water → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Utility)
Cooling water → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Utility)
Cooling water → Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) (Utility)
Cooling water → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Utility)
Cooling water → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Utility)
Cooling water → Methylamines (MMA, DMA, TMA) from methanol and ammonia (Utility)
Cooling water → Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) (Utility)
Cooling water → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Utility)
Cooling water → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Utility)
Cooling water → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Utility)
Cooling water → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Utility)
Cooling water → Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) (Utility)
Cooling water → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Utility)
Cooling water → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Utility)
Cooling water → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Utility)
Cooling water → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Utility)
Cooling water → Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) (Utility)
Cooling water → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Utility)
Cooling water → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Utility)
Cooling water → Chilled water at 6 degC from an electric chiller (Utility)
Cooling water → Instrument air, dried, 8 bar(a) (Utility)
Crude glycerol → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Feedstock)
Cumene → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Feedstock)
Dimethylamine → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Feedstock)
Disodium hydrogen phosphate → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Electricity → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Utility)
Electricity → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Utility)
Electricity → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Utility)
Electricity → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Utility)
Electricity → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Utility)
Electricity → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Utility)
Electricity → Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Utility)
Electricity → Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) (Utility)
Electricity → Cryogenic air separation unit (500 t/d GOX) (Utility)
Electricity → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Utility)
Electricity → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Utility)
Electricity → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Utility)
Electricity → Cumene by zeolite alkylation of benzene with propylene (Utility)
Electricity → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Utility)
Electricity → Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) (Utility)
Electricity → Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene (Utility)
Electricity → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Utility)
Electricity → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Utility)
Electricity → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Utility)
Electricity → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Utility)
Electricity → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Utility)
Electricity → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Utility)
Electricity → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Utility)
Electricity → Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) (Utility)
Electricity → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Utility)
Electricity → Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) (Utility)
Electricity → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Utility)
Electricity → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Utility)
Electricity → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Utility)
Electricity → Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) (Utility)
Electricity → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Utility)
Electricity → Methylamines (MMA, DMA, TMA) from methanol and ammonia (Utility)
Electricity → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Utility)
Electricity → Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) (Utility)
Electricity → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Utility)
Electricity → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Utility)
Electricity → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Utility)
Electricity → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Utility)
Electricity → Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) (Utility)
Electricity → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Utility)
Electricity → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Utility)
Electricity → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Utility)
Electricity → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Utility)
Electricity → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Utility)
Electricity → Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) (Utility)
Electricity → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Utility)
Electricity → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Utility)
Electricity → Chilled water at 6 degC from an electric chiller (Feedstock)
Electricity → Cooling water, evaporative cooling tower, 25/35 degC (Utility)
Electricity → Instrument air, dried, 8 bar(a) (Utility)
Electricity → Steam generation, natural-gas boiler, saturated 11 bar(a) (Utility)
Electricity → Wastewater treatment, activated sludge (Utility)
Ethane → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Feedstock)
Ethylbenzene → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Feedstock)
Ethylene → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Feedstock)
Ethylene → Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) (Feedstock)
Ethylene → Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene (Feedstock)
Ethylene → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Feedstock)
Waste gas to flare → Flaring of methane-rich waste gas (Feedstock)
Hydrogen → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Reactant)
Hydrogen → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Reactant)
Hydrogen → Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) (Feedstock)
Hydrogen → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Feedstock)
Hydrogen → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Feedstock)
Hydrogen → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Feedstock)
Hydrogen → Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) (Feedstock)
Hydrogen → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Feedstock)
Hydrogen → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Hydrogen → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Feedstock)
Hydrogen chloride → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Feedstock)
Hydrogen chloride → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Hydrogen chloride → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Feedstock)
Hydrogen chloride → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Feedstock)
Hydrogen peroxide → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Hydrogen peroxide → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Iodomethane (methyl iodide) → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Feedstock)
Limestone → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Manganese dioxide → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Feedstock)
Metallurgical coke → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Methane → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Feedstock)
Methane → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Feedstock)
Methane → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Methane → Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Feedstock)
Methane → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Feedstock)
Methane → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Feedstock)
Methane → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Feedstock)
Methane → Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) (Feedstock)
Methane → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Methane → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Feedstock)
Methane → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Feedstock)
Methane → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Feedstock)
Methane → Steam generation, natural-gas boiler, saturated 11 bar(a) (Feedstock)
Methanol → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Feedstock)
Methanol → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Feedstock)
Methanol → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Feedstock)
Methanol → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Feedstock)
Methanol → Methylamines (MMA, DMA, TMA) from methanol and ammonia (Feedstock)
Methyl tert-butyl ether (MTBE) → Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) (Feedstock)
N-Methyl-2-pyrrolidone → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Feedstock)
Nitric acid → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Feedstock)
Nitrobenzene → Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) (Feedstock)
Nitrogen → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Feedstock)
Nitrogen → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Feedstock)
Nitrogen → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Utility)
Oxygen → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Feedstock)
Oxygen → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Feedstock)
Oxygen → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Feedstock)
Oxygen → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Oxygen → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Oxygen → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Feedstock)
p-Toluenesulfonic acid → Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) (Feedstock)
Petroleum coke → Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) (Feedstock)
Phosphorus → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Feedstock)
Potassium hydroxide → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Feedstock)
Propylene → Cumene by zeolite alkylation of benzene with propylene (Feedstock)
Raw natural gas → Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) (Feedstock)
Silicon dioxide → Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) (Feedstock)
Sodium carbonate → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Sodium carbonate → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Feedstock)
Sodium chloride → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Sodium chloride → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Sodium hydroxide → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Feedstock)
Sodium hydroxide → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Sodium hydroxide → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Feedstock)
Sodium hydroxide → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Feedstock)
Sodium hydroxide → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Feedstock)
Sodium hydroxide → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Sodium hydroxide → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Feedstock)
Sodium hydroxide → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Feedstock)
Sodium hydroxide → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Feedstock)
Sodium hydroxide → Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) (Feedstock)
Sodium hydroxide → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Feedstock)
Sodium methoxide → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Feedstock)
Sodium methoxide → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Feedstock)
Sodium sulfate → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Sodium sulfite → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Steam → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Utility)
Steam → Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Utility)
Steam → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Utility)
Steam → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Utility)
Steam → Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) (Utility)
Steam → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Utility)
Steam → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Utility)
Steam → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Utility)
Steam → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Utility)
Steam → Cumene by zeolite alkylation of benzene with propylene (Utility)
Steam → N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) (Utility)
Steam → Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) (Utility)
Steam → Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene (Utility)
Steam → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Utility)
Steam → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Utility)
Steam → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Co-product)
Steam → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Utility)
Steam → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Utility)
Steam → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Utility)
Steam → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Utility)
Steam → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Utility)
Steam → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Utility)
Steam → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Utility)
Steam → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Utility)
Steam → Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) (Utility)
Steam → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Co-product)
Steam → Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Utility)
Steam → Methylamines (MMA, DMA, TMA) from methanol and ammonia (Utility)
Steam → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Utility)
Steam → Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) (Utility)
Steam → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Utility)
Steam → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Utility)
Steam → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Utility)
Steam → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Utility)
Steam → Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Utility)
Steam → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Utility)
Steam → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Co-product)
Steam → Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) (Utility)
Steam → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Utility)
Steam → Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) (Utility)
Succinimide → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Feedstock)
Sulfur → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Feedstock)
Sulfur → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Feedstock)
Sulfur dioxide → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Feedstock)
Sulfur dioxide → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Feedstock)
Sulfuric acid → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Feedstock)
Sulfuric acid → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Feedstock)
Sulfuric acid → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Sulfuric acid → Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) (Feedstock)
Sulfuric acid → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Sulfuric acid → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Feedstock)
Sulfuric acid → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Toluene → Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) (Feedstock)
Triethyl phosphate → Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (Feedstock)
Wastewater → Wastewater treatment, activated sludge (Feedstock)
Water → Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) (Feedstock)
Water → Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) (Feedstock)
Water → Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) (Feedstock)
Water → Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Feedstock)
Water → Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) (Feedstock)
Water → Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Feedstock)
Water → Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) (Feedstock)
Water → Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene (Feedstock)
Water → Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) (Feedstock)
Water → Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) (Feedstock)
Water → Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) (Feedstock)
Water → Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) (Feedstock)
Water → Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) (Feedstock)
Water → Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Feedstock)
Water → Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) (Feedstock)
Water → Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) (Feedstock)
Water → Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) (Feedstock)
Water → Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (Feedstock)
Water → Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) (Feedstock)
Water → Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) (Feedstock)
Water → Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) (Feedstock)
Water → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Water → N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) (Feedstock)
Water → Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) (Feedstock)
Water → Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Feedstock)
Water → Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (Feedstock)
Water → Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) (Feedstock)
Water → Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) (Feedstock)
Water → Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) (Feedstock)
Water → Styrene by adiabatic catalytic dehydrogenation of ethylbenzene (Feedstock)
Water → Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Feedstock)
Water → Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) (Feedstock)
Water → Cooling water, evaporative cooling tower, 25/35 degC (Feedstock)
Water → Steam generation, natural-gas boiler, saturated 11 bar(a) (Feedstock)
Wood chips → Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) (Feedstock)
Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) → Acetaldehyde (Main product)
Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) → Carbon dioxide (Emission)
Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a) → Wastewater (Waste)
Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) → Acetic acid (Main product)
Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) → Carbon dioxide (Waste)
Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) → Methane (Waste)
Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) → Acetic anhydride (Main product)
Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) → Carbon dioxide (Emission)
Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) → Wastewater (Waste)
Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) → Acetone (Main product)
Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) → Air (Emission)
Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) → Phenol (Co-product)
Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol) → Wastewater (Waste)
Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) → Acetylene (Main product)
Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) → Carbon dioxide (Emission)
Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) → Synthesis gas (Co-product)
Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product) → Wastewater (Waste)
Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) → Aluminium oxide (Main product)
Alumina by the Bayer process (3000 t/d smelter-grade alumina, concept) → Carbon dioxide (Emission)
Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) → Ammonia (Main product)
Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) → Carbon dioxide (Emission)
Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) → Steam (Co-product)
Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) → Wastewater (Waste)
Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) → Aniline (Main product)
Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) → Steam (Co-product)
Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h) → Wastewater (Waste)
Cryogenic air separation unit (500 t/d GOX) → Argon (Emission)
Cryogenic air separation unit (500 t/d GOX) → Nitrogen (Co-product)
Cryogenic air separation unit (500 t/d GOX) → Nitrogen (Emission)
Cryogenic air separation unit (500 t/d GOX) → Oxygen (Co-product)
Cryogenic air separation unit (500 t/d GOX) → Oxygen (Main product)
Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) → Bromine (Main product)
Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine) → Wastewater (Waste)
Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) → Carbon dioxide (Emission)
Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) → Chlorine (Main product)
Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) → Hydrogen (Co-product)
Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) → Sodium hydroxide (Co-product)
Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) → Wastewater (Waste)
Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) → Chloromethane (methyl chloride) (Main product)
Chloromethane from methanol and hydrogen chloride (gas-phase hydrochlorination, 100 kt/a) → Nitrogen (Emission)
Cumene by zeolite alkylation of benzene with propylene → Cumene (Main product)
N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) → N,N-Dimethylformamide (Main product)
N,N-Dimethylformamide by carbonylation of dimethylamine (50 kt/a, sodium methoxide in methanol) → Nitrogen (Emission)
Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) → Ethanol (Main product)
Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) → Waste gas to flare (Waste)
Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst) → Wastewater (Waste)
Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene → Ethylbenzene (Main product)
Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethylene → Wastewater (Waste)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Carbon dioxide (Emission)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Crude C4 cut (Co-product)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Ethylene (Main product)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Propylene (Co-product)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Pyrolysis gasoline (Co-product)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Steam (Co-product)
Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept) → Wastewater (Waste)
Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) → Carbon dioxide (Emission)
Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) → Diethylene glycol (Co-product)
Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) → Ethylene glycol (monoethylene glycol) (Main product)
Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) → Triethylene glycol (Co-product)
Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG) → Wastewater (Waste)
Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) → Carbon dioxide (Emission)
Formaldehyde by methanol oxidation over iron molybdate (Formox type, 20 t/h formalin 50 wt%) → Formaldehyde (Main product)
Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) → Carbon dioxide (Emission)
Formic acid 85 wt% by methanol carbonylation and methyl formate hydrolysis (50 kt/a) → Formic acid (Main product)
Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) → Glycerol (Main product)
Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) → Methanol (Co-product)
Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept) → Wastewater (Waste)
Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) → Benzene (Main product)
Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) → Biphenyl (Co-product)
Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) → Hydrogen (Co-product)
Toluene hydrodealkylation to benzene (100 kt/a, thermal HDA) → Methane (Co-product)
Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) → Hydrazine (Main product)
Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) → Oxygen (Emission)
Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) → Wastewater (Waste)
Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) → Carbon dioxide (Emission)
Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) → Hydrogen (Main product)
Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) → Steam (Co-product)
Hydrogen by natural-gas steam methane reforming with PSA (100 000 Nm3/h, steam export) → Water (Waste)
Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) → Hydrogen (Emission)
Hydrogen bromide synthesis burner with catalytic finishing and absorption (48 wt-% hydrobromic acid) → Hydrogen bromide (Main product)
Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) → Hydrogen (Emission)
Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) → Hydrogen chloride (Main product)
Hydrogen chloride synthesis burner and absorption (33 wt-% hydrochloric acid, steam recovery) → Steam (Co-product)
Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) → Hydrogen peroxide (Main product)
Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) → Nitrogen (Emission)
Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) → Wastewater (Waste)
Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) → Hydroxylammonium sulfate (Main product)
Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) → Nitrogen (Emission)
Hydroxylammonium sulfate by catalytic NO hydrogenation (30 kt/a NH2OH, 25 wt% solution) → Steam (Co-product)
Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) → Iodine (Main product)
Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a) → Wastewater (Waste)
Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) → Isobutene (2-methylpropene) (Main product)
Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) → Methanol (Co-product)
Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage) → Wastewater (Waste)
Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) → Bleached kraft pulp (Main product)
Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) → Carbon dioxide (Emission)
Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) → Electricity (Co-product)
Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept) → Wastewater (Waste)
Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) → Carbon dioxide (Emission)
Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) → Methanol (Main product)
Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) → Water (Waste)
Methylamines (MMA, DMA, TMA) from methanol and ammonia → Dimethylamine (Main product)
Methylamines (MMA, DMA, TMA) from methanol and ammonia → Methylamine (monomethylamine) (Co-product)
Methylamines (MMA, DMA, TMA) from methanol and ammonia → Trimethylamine (Co-product)
Methylamines (MMA, DMA, TMA) from methanol and ammonia → Wastewater (Waste)
N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) → N-Bromosuccinimide (Main product)
N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a) → Wastewater (Waste)
Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) → Carbon dioxide (Emission)
Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) → Methane (Emission)
Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) → Methane (Main product)
Natural gas processing (amine CO2 removal, TEG dehydration, turbo-expander NGL recovery) → Natural gas liquids (Co-product)
Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) → Nitric acid (Main product)
Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) → Nitrogen (Emission)
Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) → Steam (Co-product)
Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) → Carbon dioxide (Emission)
Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) → Phosgene (Main product)
Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) → Wastewater (Waste)
Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) → Phosphorus oxychloride (phosphoryl chloride) (Main product)
Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h) → Wastewater (Waste)
Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) → Hydrogen (Emission)
Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) → Potassium permanganate (Main product)
Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept) → Wastewater (Waste)
Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) → Carbon dioxide (Emission)
Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) → Silicon carbide (Co-product)
Silicon carbide by the Acheson process (5000 kg/h crude SiC, concept) → Silicon carbide (Main product)
Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) → Carbon dioxide (Emission)
Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) → Sodium carbonate (Main product)
Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept) → Wastewater (Waste)
Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) → Carbon dioxide (Emission)
Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) → Sodium cyanide (Main product)
Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) → Steam (Co-product)
Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a) → Wastewater (Waste)
Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) → Carbon dioxide (Emission)
Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) → Sodium nitrate (Co-product)
Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) → Sodium nitrite (Main product)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Benzene (Co-product)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Carbon dioxide (Emission)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Styrene (Main product)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Toluene (Co-product)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Wastewater (Waste)
Styrene by adiabatic catalytic dehydrogenation of ethylbenzene → Water (Emission)
Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) → Nitrogen (Emission)
Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) → Sulfuric acid (Main product)
Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) → Tetrahydrofuran (Main product)
Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation) → Wastewater (Waste)
Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) → Oxygen (Emission)
Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) → Thionyl chloride (Main product)
Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h) → Wastewater (Waste)
Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) → Urea (Main product)
Urea by CO2 stripping, total recycle, prilling (2000 t/d, concept) → Water (By-product)
Chilled water at 6 degC from an electric chiller → Chilled water (Main product)
Cooling water, evaporative cooling tower, 25/35 degC → Cooling water (Main product)
Cooling water, evaporative cooling tower, 25/35 degC → Wastewater (Waste)
Cooling water, evaporative cooling tower, 25/35 degC → Water (Emission)
Flaring of methane-rich waste gas → Carbon dioxide (Emission)
Flaring of methane-rich waste gas → Waste gas to flare (Main product)
Flaring of methane-rich waste gas → Methane (Emission)
Instrument air, dried, 8 bar(a) → Instrument air (Main product)
Instrument air, dried, 8 bar(a) → Wastewater (Waste)
Steam generation, natural-gas boiler, saturated 11 bar(a) → Carbon dioxide (Emission)
Steam generation, natural-gas boiler, saturated 11 bar(a) → Steam (Main product)
Steam generation, natural-gas boiler, saturated 11 bar(a) → Wastewater (Waste)
Steam generation, natural-gas boiler, saturated 11 bar(a) → Water (Emission)
Wastewater treatment, activated sludge → Carbon dioxide (Emission)
Wastewater treatment, activated sludge → Wastewater (Main product)
Wastewater treatment, activated sludge → Water (Emission)