Process for the extraction of hydrogen from a gas mixture
View Patent ↗A process for the extraction of hydrogen from a gas mixture including hydrogen and carbon monoxide and optionally nitrogen, carbon dioxide, lower hydrocarbons and/or water, by contacting the gas mixture with a non-porous polyimide-based membrane, especially with the selective side of an asymmetric membrane, to obtain a hydrogen rich permeate and a hydrogen lean retenate, the polyimide-based membrane being a specific mixture of two polyimids. This specific membrane shows a very high hydrogen/carbon monoxide selectivity. The process is especially suitable for the upgrading of synthesis gas obtained by partial oxidation and/or reforming of hydrocarbonaceous feedstream for use in hydrocarbon synthesis reaction as the Fischer-Tropsch reaction.
1. A process for the extraction of hydrogen from a gas mixture comprising hydrogen and carbon monoxide and optionally nitrogen, carbon dioxide, lower hydrocarbons and/or water, by contacting the gas mixture with a non-porous polyimide-based membrane, to obtain a hydrogen rich permeate and a hydrogen lean retentate, the membrane being a blend of BTDA-DAPI and BTDA-TDI/MDI.
2. A process according to claim 1 , in which the amount of BTDA-DAPI is between 20 and 80 wt % of the membrane and the amount of BTDA-TDI/MDI is between 80 and 20 wt % of the membrane.
3. A process according to claim 1 in which the total amount of hydrogen and carbon monoxide in the gas mixture is between 20 and 100 vol % (based on the total volume of gas mixture).
4. A process according to claim 1 , in which the hydrogen/carbon monoxide molar ratio is between 0.3 and 10.
5. A process according to claim 1 , in which also carbon dioxide is present in the gas mixture in an amount of between 0 and 20 vol % (based on the total volume of gas mixture).
6. A process according to claim 1 , in which the amount of water is up till 2 vol %.
7. A process according to claim 1 , in which the extraction is carried out at a temperature between 10 and 120° C.
8. A process according to claim 1 , in which the extraction is carried out with a pressure difference over the membrane of between 2 and 100 bar.
9. A process according to claim 1 , in which the pressure of the permeate is between 0.1 and 20 bar (absolute).
10. A process according to claim 1 , in which the pressure of the gas mixture is between 2.1 and 120 bar (absolute).
11. A process according to claim 1 , in which the gas mixture is synthesis gas obtained by partial oxidation and/or reforming of a hydrocarbonaceous feedstock, the synthesis gas being subjected to a water-gas shift reaction to increase the amount of hydrogen and to decrease the amount of carbon monoxide, the water-gas shift reaction comprising a hot and a cold water-gas shift reaction.
12. A process according to claim 1 , in which the synthesis gas is synthesis gas from which compounds other than hydrogen, carbon monoxide, water, nitrogen and carbon dioxide have been removed.
13. A process according to claim 1 , in which the hydrogen rich permeate is further purified by pressure swing adsorption.
14. A process for the preparation of hydrocarbons from synthesis gas by means of a hydrocarbon synthesis reaction, the synthesis gas being made by partial oxidation of a hydrocarbonaceous feedstock, the synthesis gas having an H 2 /CO ratio below the consumption ratio of the hydrocarbon synthesis reaction, in which hydrogen is extracted from the synthesis gas by the extraction of hydrogen from a gas mixture comprising hydrogen and carbon monoxide and optionally nitrogen, carbon dioxide, lower hydrocarbons and/or water, by contacting the gas mixture with a non-porous polyimide-based membrane, to obtain a hydrogen rich permeate and a hydrogen lean retentate, the membrane being a blend of BTDA-DAPI and BTDA-TDI/MDI, and using a part of the hydrogen lean retentate, and hydrogen rich permeate in the hydrocarbon synthesis reaction.
15. A process for the preparation of hydrocarbons from synthesis gas by means of a hydrocarbon synthesis reaction, the synthesis gas being made by reforming of a hydrocarbonaceous feedstock in combination with partial oxidation, the synthesis gas having an H2/CO ratio above the consumption ratio of the hydrocarbon synthesis reaction, in which hydrogen is extracted from the synthesis gas by the extraction of hydrogen from a gas mixture comprising hydrogen and carbon monoxide and optionally nitrogen, carbon dioxide, lower hydrocarbons and/or water, by contacting the gas mixture with a non-porous polyimide-based membrane, to obtain a hydrogen rich permeate and a hydrogen lean retentate, the membrane being a blend of BTDA-DAPI and BTDA-TDI/MDI, and using the hydrogen lean retentate in the hydrocarbon synthesis reaction.