IPC분류정보
| 국가/구분 |
United States(US) Patent
등록
|
| 국제특허분류(IPC7판) |
|
| 출원번호 |
US-0906552
(2010-10-18)
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| 등록번호 |
US-8479834
(2013-07-09)
|
|
발명자
/ 주소 |
|
| 출원인 / 주소 |
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| 대리인 / 주소 |
McDonnell Boehnen Hulbert & Berghoff LLP
|
| 인용정보 |
피인용 횟수 :
15 인용 특허 :
201 |
초록
An enhanced oil recovery process that is integrated with a synthesis gas generation process, such as gasification or methane reforming, involving combined capture and recycle of carbon dioxide from both processes.
대표청구항
▼
1. An integrated process to (i) produce an acid gas-depleted gaseous hydrocarbon product steam, (ii) produce a liquid hydrocarbon product stream and (iii) enhance production of a hydrocarbon-containing fluid from an underground hydrocarbon reservoir, the process comprising the steps of: (1) injectin
1. An integrated process to (i) produce an acid gas-depleted gaseous hydrocarbon product steam, (ii) produce a liquid hydrocarbon product stream and (iii) enhance production of a hydrocarbon-containing fluid from an underground hydrocarbon reservoir, the process comprising the steps of: (1) injecting a pressurized carbon dioxide stream into an underground hydrocarbon reservoir to enhance production of the hydrocarbon-containing fluid from the underground hydrocarbon reservoir via a hydrocarbon production well, the hydrocarbon-containing fluid comprising carbon dioxide;(2) recovering the hydrocarbon-containing fluid produced from the hydrocarbon production well;(3) separating the hydrocarbon-containing fluid into (a) the liquid hydrocarbon product stream and (b) a gaseous hydrocarbon stream comprising carbon dioxide;(4) producing a synthesis gas stream from a carbonaceous feedstock, the synthesis gas stream comprising (a) at least one of carbon monoxide and carbon dioxide, and (b) at least one of hydrogen and methane;(5) co-treating the gaseous hydrocarbon stream and the synthesis gas stream in an acid gas removal system to produce the acid gas-depleted gaseous hydrocarbon product stream and a carbon dioxide-rich recycle stream; and(6) pressurizing the carbon dioxide-rich recycle stream to generate the pressurized carbon dioxide stream. 2. The process of claim 1, wherein the carbonaceous feedstock is a gaseous methane-containing stream, and step (4) comprises the step of converting the gaseous methane-containing stream in a catalytic steam methane reforming process to a syngas as the synthesis gas stream. 3. The process of claim 2, wherein the methane-containing stream comprises at least a portion of the acid-gas depleted gaseous hydrocarbon product stream. 4. The process of claim 1, wherein the carbonaceous feedstock is a gaseous methane-containing stream, and step (4) comprises the step of converting the gaseous methane-containing stream in a non-catalytic gaseous partial oxidation process to produce a syngas as the synthesis gas stream. 5. The process of claim 4, wherein the methane-containing stream comprises at least a portion of the acid-gas depleted gaseous hydrocarbon product stream. 6. The process of claim 1, wherein the carbonaceous feedstock is a gaseous methane-containing stream, and step (4) comprises the step of converting the gaseous methane-containing stream in a catalytic autothermal reforming process to produce a syngas as the synthesis gas stream. 7. The process of claim 6, wherein the methane-containing stream comprises at least a portion of the acid-gas depleted gaseous hydrocarbon product stream. 8. The process of claim 1, wherein the carbonaceous feedstock is a non-gaseous carbonaceous material, and step (4) comprises the step of converting the non-gaseous carbonaceous material in a non-catalytic thermal gasification process to produce a syngas as the synthesis gas stream. 9. The process of claim 1, wherein the synthesis gas stream comprises hydrogen and one or both of carbon monoxide and carbon dioxide. 10. The process of claim 1, wherein the carbonaceous feedstock is a non-gaseous carbonaceous material, and step (4) comprises the step of converting the non-gaseous carbonaceous material in a catalytic hydromethanation process to produce a methane-enriched gas stream as the synthesis gas stream. 11. The process of claim 1, wherein the synthesis gas stream comprises methane, hydrogen and carbon dioxide. 12. The process of claim 1, wherein at least a portion of the synthesis gas stream is subject to a sour shift to generate a hydrogen-enriched stream. 13. The process of claim 1, wherein the acid-gas depleted gaseous hydrocarbon product stream comprises hydrogen, and at least a portion of the hydrogen is separated to generate a hydrogen product stream and a hydrogen-depleted gas stream. 14. The process of claim 1, wherein the acid-gas depleted gaseous hydrocarbon product stream comprises hydrogen and carbon monoxide, and is subject to a methanation to produce a methane-enriched gas stream. 15. The process of claim 1, wherein the synthesis gas stream and the gaseous hydrocarbon stream are combined and subject to a dehydration prior to acid gas removal. 16. The process of claim 1, wherein the synthesis gas stream and the gaseous hydrocarbon stream are separately subject to a dehydration and combined prior to acid gas removal. 17. The process of claim 1, wherein the synthesis gas stream and the gaseous hydrocarbon stream are combined and co-processed during acid gas removal. 18. A process to enhance production of a hydrocarbon-containing fluid from an underground hydrocarbon reservoir via a hydrocarbon production well by injecting a pressurized carbon dioxide stream into an underground hydrocarbon reservoir, wherein the hydrocarbon-containing fluid comprises carbon dioxide, and wherein the pressurized carbon dioxide stream is generated by a process comprising the steps of: (I) recovering the hydrocarbon-containing fluid produced from the hydrocarbon production well;(II) splitting the hydrocarbon-containing fluid into (a) a liquid hydrocarbon product stream and (b) a gaseous hydrocarbon stream comprising carbon dioxide;(III) producing a synthesis gas stream from a carbonaceous feedstock, the synthesis gas stream comprising (a) at least one of carbon monoxide and carbon dioxide, and (b) at least one of hydrogen and methane;(IV) co-treating the gaseous hydrocarbon stream and the synthesis gas stream in an acid gas removal system to produce an acid gas-depleted gaseous hydrocarbon product stream and a carbon dioxide-rich recycle stream; and(V) pressurizing the carbon dioxide-rich recycle stream to generate the pressurized carbon dioxide stream. 19. An apparatus for generating a liquid hydrocarbon product stream and an acid gas-depleted gaseous hydrocarbon product stream, the apparatus comprising: (A) a synthesis gas production system adapted for producing a synthesis gas from a carbonaceous feedstock, the synthesis gas comprising (i) at least one of carbon monoxide and carbon dioxide, and (ii) at least one of hydrogen and methane;(B) a carbon dioxide injection well in fluid communication with an underground hydrocarbon reservoir, the carbon dioxide injection well adapted for injecting a pressurized carbon dioxide stream into the underground hydrocarbon reservoir for enhanced oil recovery;(C) a hydrocarbon production well in fluid communication with the underground hydrocarbon reservoir, the hydrocarbon production well being adapted for removing a hydrocarbon fluid from the underground hydrocarbon reservoir, the hydrocarbon fluid comprising carbon dioxide;(D) a separation device in fluid communication with the hydrocarbon production well, the separation device adapted (i) to receive the hydrocarbon fluid from the hydrocarbon production well, and (ii) to separate the hydrocarbon fluid into the liquid hydrocarbon product stream and a gaseous hydrocarbon stream comprising carbon dioxide;(E) an acid gas removal system in fluid communication with the synthesis gas production system and the liquid/gas separation device, the acid gas removal system adapted to (i) receive the synthesis gas from the synthesis gas production system and the gaseous hydrocarbon stream from the liquid/gas separation device, and (ii) co-treat the synthesis gas stream and gaseous hydrocarbon stream to remove acid gases and produce the acid gas-depleted gaseous hydrocarbon product stream and a carbon dioxide-rich recycle stream; and(F) a compressor unit in fluid communication with the acid gas removal system and the carbon dioxide injection well, the compressor unit adapted to (i) receive the carbon dioxide-rich recycle stream, and (ii) compress the carbon dioxide recycle stream to generate the pressurized carbon dioxide stream, and (iii) provide the pressurized carbon dioxide stream to the carbon dioxide injection well. 20. The apparatus of claim 19, further comprising a sour shift unit between the synthesis gas production system and the acid gas removal system.
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