Gasification process

Abstract

The present invention provides integrated process for the production of a useful liquid hydrocarbon product comprising the steps of: feeding a gasification zone with an oxygen-containing feed and a first carbonaceous feedstock comprising waste materials and/or biomass, gasifying the first carbonaceous feedstock in the gasification zone to produce a first synthesis gas, partially oxidising the first synthesis gas in a partial oxidation zone to generate partially oxidised synthesis gas, combining at least a portion of the first synthesis gas and/or the partially oxidised synthesis gas and at least a portion of electrolysis hydrogen obtained from an electrolyser in an amount to achieve the desired hydrogen to carbon monoxide molar ratio of from about 1.5:1 to about 2.5:1, which is higher than that of the first synthesis gas, and to generate a blended synthesis gas, wherein the electrolyser operates using green electricity; and subjecting at least a portion of the blended synthesis gas to a conversion process effective to produce the liquid hydrocarbon product.

1 . An integrated process for the production of a useful liquid hydrocarbon product comprising the steps of:
 feeding a gasification zone with an oxygen-containing feed and a first carbonaceous feedstock comprising waste materials and/or biomass,   gasifying the first carbonaceous feedstock in the gasification zone to produce a first synthesis gas,   partially oxidising the first synthesis gas in a partial oxidation zone to generate partially oxidised synthesis gas,   combining at least a portion of the first synthesis gas and/or the partially oxidised synthesis gas and at least a portion of electrolysis hydrogen obtained from an electrolyser in an amount to achieve a desired hydrogen to carbon monoxide molar ratio of from about 1.5:1 to about 2.5:1, which is higher than that of the first synthesis gas, and to generate a blended synthesis gas, wherein the electrolyser operates using green electricity; and   subjecting at least a portion of the blended synthesis gas to a conversion process effective to produce the liquid hydrocarbon product.   
     
     
         2 . The process according to  claim 1  wherein the oxygen-containing feed comprises electrolysis oxygen obtained from the electrolyser. 
     
     
         3 . The process according to  claim 1  wherein at least a portion of the first synthesis gas and/or partially oxidised synthesis gas is decontaminated in a clean-up zone to generate clean synthesis gas. 
     
     
         4 . The process according to  claim 3  wherein the clean-up zone comprises the removal of ammoniacal, sulphurous and carbon dioxide impurities, preferably sequentially. 
     
     
         5 . The process according to  claim 1  wherein the desired hydrogen to carbon molar ratio of the blended synthesis gas is from about 1.7:1 to about 2.2:1, or preferably from about 1.95:1 to about 2.05:1. 
     
     
         6 . The process according to  claim 1  wherein the useful liquid hydrocarbon product is produced by subjecting at least part of the blended synthesis gas to a Fischer-Tropsch synthesis. 
     
     
         7 . The process according to  claim 6  wherein the blended synthesis gas is converted by Fischer-Tropsch synthesis into liquid hydrocarbons. 
     
     
         8 . The process according to  claim 7  wherein the liquid hydrocarbons are upgraded into the useful liquid hydrocarbon product. 
     
     
         9 . The process according to  claim 8  wherein at least a part of the liquid hydrocarbons are upgraded by at least one of hydroprocessing, product fractionation, hydrocracking and/or hydroisomerisation to produce the useful product. 
     
     
         10 . The process according to  claim 1  wherein the product comprises synthetic paraffinic kerosene and/or diesel and/or naphtha,
 optionally—wherein the synthetic paraffinic kerosene and/or diesel and/or naphtha is combined with another fuel component to make a transportation fuel. 
 
     
     
         11 . The process according to  claim 1  wherein the process is further integrated with a reforming process. 
     
     
         12 . The process according to  claim 1  wherein the process further comprises reforming a second carbonaceous feedstock to produce a second synthesis gas. 
     
     
         13 . The process according to  claim 12  wherein the reforming step is at least one of steam methane reforming and autothermal reforming. 
     
     
         14 . The process according to  claim 12  wherein the second carbonaceous feedstock comprises gas wherein the gas is at least one of natural gas, renewable natural gas, biogas, low-carbon methanol and low carbon ethanol. 
     
     
         15 . The process according to  claim 12  wherein the first synthesis gas is subjected to partial oxidation and the second carbonaceous feedstock, preferably renewable natural gas, is combusted in the partial oxidation zone. 
     
     
         16 . The process according  claim 12  wherein the blended synthesis gas comprises combining at least a portion of the second synthesis gas with at least a portion of the partially oxidised synthesis gas and/or at least a portion of the clean synthesis gas and/or at least a portion of the electrolysis hydrogen in an amount to achieve the desired hydrogen to carbon monoxide molar ratio. 
     
     
         17 . The process according to  claim 1  wherein the process further comprises combining green hydrogen with at least one of electrolysis hydrogen and/or partially oxidised synthesis gas and/or clean synthesis gas and/or second synthesis gas. 
     
     
         18 . The process according to  claim 1  wherein the process comprises at least 2 different renewable feedstocks, at least 3 different renewable feedstocks or at least 4 different renewable feedstocks. 
     
     
         19 . The process according to  claim 18  wherein the renewable feedstock comprises waste and/or biomass and/or green electricity and/or green hydrogen and/or renewable natural gas.