Process for the preparation and conversion of synthesis gas
View Patent ↗A process ( 10 ) for the preparation and conversion of synthesis gas includes reforming a feed gas ( 34 ) comprising methane in a reforming stage ( 18 ) to produce synthesis gas ( 46 ) which includes hydrogen and carbon monoxide. Some of the hydrogen and carbon monoxide is converted to a Fischer-Tropsch product ( 48 ) in a Fischer-Tropsch hydrocarbon synthesis stage ( 24 ). A tail gas ( 52 ), including unreacted hydrogen and carbon monoxide, methane and carbon dioxide, is separated from the Fischer-Tropsch product ( 48 ). In a tail gas treatment stage ( 28,30 ), the tail gas ( 52 ) is treated by reforming the methane in the tail gas ( 52 ) with steam ( 66 ) and removing carbon dioxide to produce a hydrogen rich gas ( 56 ). The tail gas treatment stage ( 28,30 ) may be either a combined tail gas treatment stage ( 28,30 ) or a composite tail gas treatment stage. The carbon dioxide from the tail gas treatment stage ( 28,30 ) is fed to the reforming stage ( 18 ).
1. A process for the preparation and conversion of synthesis gas which includes
in a feed gas reforming stage, reforming a feed gas which includes methane to produce synthesis gas which includes hydrogen and carbon monoxide;
in a Fischer-Tropsch hydrocarbon synthesis stage, converting some of the hydrogen and carbon monoxide into a Fischer-Tropsch product;
separating a tail gas which includes unreacted hydrogen and carbon monoxide, methane and carbon dioxide, from the Fischer-Tropsch product;
in a tail gas treatment stage which includes methane reforming and water gas shift catalyst, and carbon dioxide sorbent, treating the tail gas by reforming the methane in the tail gas in the presence of steam to produce hydrogen and carbon dioxide, with at least some of the carbon dioxide being absorbed or adsorbed by the carbon dioxide sorbent to produce a hydrogen rich gas; and
from time to time, desorbing the carbon dioxide from the carbon dioxide sorbent and feeding the carbon dioxide to the feed gas reforming stage in which the feed gas is reformed.
2. The process as claimed in claim 1 , which includes at least two of the tail gas treatment stages, with at least one of the tail gas treatment stages being used to treat the tail gas to produce the hydrogen rich gas, while at least one of the other tail gas treatment stages is being used to produce carbon dioxide for feeding to the feed gas reforming stage by desorbing the carbon dioxide from the carbon dioxide sorbent.
3. The process as claimed in claim 1 , in which the methane reforming and water gas shift catalyst, and the carbon dioxide sorbent are in the form of a composite material.
4. The process as claimed in claim 3 , in which the composite material has a carbon dioxide sorbent core encased in a porous shell that serves as a catalyst support.
5. The process as claimed in claim 1 , in which the tail gas treatment stage is operated at a temperature of at least about 350° C. and of not more than about 650° C. when treating the tail gas to produce the hydrogen rich gas.
6. The process as claimed in claim 1 , in which the carbon dioxide is desorbed or stripped from the carbon dioxide sorbent by a stripping gas at a temperature of at least about 650° C.
7. The process as claimed in claim 6 , in which the stripping gas is reformer feed gas or partially reformed reformer feed gas.
8. The process as claimed in claim 1 , in which the feed gas reforming stage includes a gas heated reformer or heat exchange reformer, and an autothermal reformer, with the synthesis gas from the autothermal reformer being used to provide heat for the reforming reactions taking place in the gas heated reformer, and wherein the carbon dioxide from the tail gas treatment stage is fed to the autothermal reformer.
9. The process as claimed in claim 8 , in which a stripping gas is used to desorb carbon dioxide from the sorbent, and in which the stripping gas is partially reformed feed gas from the gas heated reformer.
10. The process as claimed in claim 1 , in which a portion of the hydrogen rich gas is added to the synthesis gas from the feed gas reforming stage to adjust the molar ratio of hydrogen and carbon monoxide in the synthesis gas.
11. The process as claimed in claim 1 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and which includes recycling at least some of the high purity hydrogen stream to the Fischer-Tropsch hydrocarbon synthesis stage.
12. The process as claimed in claim 1 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and in which purged tail gas from the Fischer-Tropsch hydrocarbon synthesis stage is combined with at least a portion of the high purity hydrogen stream, and/or with at least a portion of the hydrogen rich gas to produce a synthesis gas suitable for methanol synthesis and/or di-methyl-ether (DME) synthesis and/or Fischer-Tropsch hydrocarbon synthesis.
13. The process as claimed in claim 1 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and in which the hydrogen rich gas and/or high purity hydrogen stream is used together with nitrogen from an air separation unit to produce ammonia.
14. The process as claimed in claim 1 , which includes a hydrogenation stage in which unsaturated compounds in the tail gas are hydrogenated upstream of the tail gas treatment stage.
15. A process for the preparation and conversion of synthesis gas which includes
in a feed gas reforming stage, reforming a feed gas which includes methane to produce synthesis gas which includes hydrogen and carbon monoxide;
in a Fischer-Tropsch hydrocarbon synthesis stage, converting some of the hydrogen and carbon monoxide into Fischer-Tropsch product;
separating a tail gas which includes unreacted hydrogen and carbon monoxide, methane and carbon dioxide, from the Fischer-Tropsch product;
in a tail gas treatment stage, treating the tail gas by reforming the methane in the tail gas in the presence of steam to produce a reformed tail gas which includes hydrogen, carbon dioxide and carbon monoxide, and thereafter removing carbon dioxide from the reformed tail gas to produce a hydrogen rich gas and a carbon dioxide rich stream; and
feeding the carbon dioxide rich stream to the feed gas reforming stage in which the feed gas is reformed.
16. The process as claimed in claim 15 , in which the feed gas reforming stage includes a gas heated reformer or heat exchange reformer, and an autothermal reformer, with the synthesis gas from the autothermal reformer being used to provide heat for the reforming reactions taking place in the gas heated reformer, and wherein the carbon dioxide from the tail gas treatment stage is fed to the autothermal reformer.
17. The process as claimed in claim 16 , in which a stripping gas is used to desorb carbon dioxide from the sorbent, and in which the stripping gas is partially reformed feed gas from the gas heated reformer.
18. The process as claimed in claim 15 , in which a portion of the hydrogen rich gas is added to the synthesis gas from the feed gas reforming stage to adjust the molar ratio of hydrogen and carbon monoxide in the synthesis gas.
19. The process as claimed in claim 15 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and which includes recycling at least some of the high purity hydrogen stream to the Fischer-Tropsch hydrocarbon synthesis stage.
20. The process as claimed in claim 15 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and in which purged tail gas from the Fischer-Tropsch hydrocarbon synthesis stage is combined with at least a portion of the high purity hydrogen stream, and/or with at least a portion of the hydrogen rich gas to produce a synthesis gas suitable for methanol synthesis and/or di-methyl-ether (DME) synthesis and/or Fischer-Tropsch hydrocarbon synthesis.
21. The process as claimed in claim 15 , in which a portion of the hydrogen rich gas is further purified to produce a high purity hydrogen stream, and in which the hydrogen rich gas and/or high purity hydrogen stream is used together with nitrogen from an air separation unit to produce ammonia.
22. The process as claimed in claim 15 , in which the tail gas treatment stage includes converting the carbon monoxide in the reformed tail gas using water gas shift reaction to produce hydrogen and carbon dioxide; and in which the carbon dioxide rich steam is compressed before feeding to the feed gas reforming stage.
23. The process as claimed in claim 15 , which includes a hydrogenation stage in which unsaturated compounds in the tail gas are hydrogenated upstream of the tail gas treatment stage.
24. A process for the preparation and conversion of synthesis gas which includes
in a reforming stage, reforming a feed gas which includes methane to produce synthesis gas which includes hydrogen and carbon monoxide;
in a Fischer-Tropsch hydrocarbon synthesis stage, converting some of the hydrogen and carbon monoxide into a Fischer-Tropsch product;
separating a tail gas which includes unreacted hydrogen and carbon monoxide, methane and carbon dioxide, from the Fischer-Tropsch product;
in a tail gas treatment stage which includes methane reforming and water gas shift catalyst, and carbon dioxide sorbent, treating the tail gas by reforming the methane in the tail gas in the presence of steam to produce hydrogen and carbon dioxide, with at least some of the carbon dioxide being absorbed or adsorbed by the carbon dioxide sorbent to produce a hydrogen rich gas, the methane reforming and water gas shift catalyst, and the carbon dioxide sorbent being in the form of a composite material; and
from time to time, desorbing the carbon dioxide from the carbon dioxide sorbent and feeding the carbon dioxide to the reforming stage.
25. The process as claimed in claim 24 , in which the composite material has a carbon dioxide sorbent core encased in a porous shell that serves as a catalyst support.