Process for the production of synthesis gas with conversion of CO2 into hydrogen
Process for the production of liquid hydrocarbons from a feedstock that comprises at least one elementary feedstock from the group of biomass, coal, lignite, petroleum residues, methane, and natural gas, comprising: at least one stage a) for gasification of the feedstock by partial oxidation and/or steam reforming to produce a synthesis gas SG; a stage b) for separating CO2 from SG and a portion of the effluent of the subsequent stage c); the mixing of a portion of the CO2 that is separated with a gas of an H2/CO ratio of more than 3; a stage c) for partial conversion with hydrogen, thermal or thermocatalytic, of the CO2 that is present in said first mixture according to the reaction: CO2+H2→CO+H2O in a specific reaction zone that is separated from said gasification zone or zones; a stage d) for Fisher-Tropsch synthesis on a synthesis gas that comprises at least a portion of SG and at least a portion of the CO that is produced by the conversion of CO2 into hydrogen.
1. A process for producing liquid hydrocarbons from a feedstock that comprises at least one elementary feedstock from the group of biomass, coal, lignite, petroleum residues that boil essentially above 340° C., methane, and natural gas, said process comprising at least:
a stage a) for gasification of said feedstock by partial oxidation in the presence of oxygen and/or steam reforming, in a gasification or zone of gasification, for the production of CO2 and a synthesis gas (SG) effluent comprising H 2 and CO;
a stage b) for separating CO2 from SG, and/or at least a portion of the effluent of the subsequent stage c);
a stage for mixing at least a portion of the CO2 that is separated with a gas with an H2/CO ratio that is more than 3 and is derived from at least one of (A) a gaseous effluent from steam reforming of methane or natural gas, and (B) hydrogen that is produced by electrolysis of water, as well as by mixtures thereof, to obtain a first mixture that comprises CO2 and hydrogen;
a stage c) for partial conversion with hydrogen, thermal or thermocatalytic, of the CO2 present in said first mixture according to the reaction: CO2+H2→CO+H2O in a specific reaction zone that is separated from said gasification zone;
a stage d) for Fischer-Tropsch synthesis of hydrocarbons that have mostly at least 5 carbon atoms from a synthesis gas that comprises at least a portion of effluents of stage c).
2. A process according to claim 1 , in which said gas with an H2/CO ratio of more than 3 comprises an effluent from steam reforming of a light feedstock that primarily comprises methane and/or natural gas.
3. A process according to claim 2 , in which said gas with an H2/CO ratio of more than 3 comprises an uncooled effluent from steam reforming of a light feedstock that comprises primarily methane and/or natural gas, at a temperature of more than 750° C., to which CO2 that is preheated to at least 250° C. is added to obtain said first mixture, and said first mixture is injected into effluent SG that is at a temperature of between 1250° C. and 1600° C. to obtain a second mixture at a temperature of between 900° C. and 1200° C. that is subjected to stage c) for the thermal or thermocatalytic reaction of partial conversion with hydrogen of the CO2 that is present in this mixture according to the reaction: CO2+H2→CO+H2O in an adiabatic reaction zone.
4. A process according to claim 3 , in which the feedstock of the gasification stage a) is a light feedstock that primarily comprises methane and/or natural gas, and the stage c) is carried out on a catalyst that comprises nickel at an outlet temperature of between 900° C. and 1100° C.
5. A process according to claim 3 , in which stage c) is carried out without a catalyst, at an outlet temperature of between 1050° C. and 1200° C.
6. A process according to claim 1 , in which said gas with an H2/CO ratio of more than 3 comprises a steam-reforming effluent of a light feedstock that primarily comprises methane and/or natural gas and that has been cooled to condense at least a portion of the water that is contained in this effluent.
7. A process according to claim 1 , in which an electrolysis of water is carried out to produce hydrogen and oxygen; at least a portion of the hydrogen that is produced is used to compose said gas with an H2/CO ratio of more than 3, and at least a portion of the oxygen is used for the gasification stage a).
8. A process according to claim 2 , in which said feedstock comprises both a light feedstock that comprises primarily methane, and a heavy feedstock that comprises coal and/or lignite and/or the lignocellulosic biomass and/or a petroleum residue.
9. A process according to claim 2 , in which said gas with an H2/CO ratio of more than 3 comprises a steam-reforming effluent of a light feedstock that primarily comprises methane and/or natural gas and that has been cooled to condense at least a portion of the water that is contained in this effluent.
10. A process according to claim 3 , in which said feedstock comprises both a light feedstock that comprises primarily methane, and a heavy feedstock that comprises coal and/or lignite and/or the lignocellulosic biomass and/or a petroleum residue.
11. A process according to claim 5 , in which said feedstock comprises both a light feedstock that comprises primarily methane, and a heavy feedstock that comprises coal and/or lignite and/or the lignocellulosic biomass and/or a petroleum residue.