[특허]Downhole separation of carbon dioxide from natural gas produced from natural gas reservoirs

Schlumberger Technology Corporation

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특허 상세정보

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Downhole separation of carbon dioxide from natural gas produced from natural gas reservoirs

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	B01D-053/02
미국특허분류(USC)	095/096; 095/139; 096/121
출원번호	UP-0956414 (2007-12-14)
등록번호	US-7763099 (2010-08-13)
발명자 / 주소	Verma, Sandeep Ramakrishnan, Terizhandur S.
출원인 / 주소	Schlumberger Technology Corporation
대리인 / 주소	Loccisano, Vincent
인용정보	피인용 횟수 : 19 인용 특허 : 2

초록

Methods and systems are provided where a production gas stream including natural gas and carbon dioxide is separated downhole using dual reflux pressure swing adsorption with the natural gas being produced and the carbon dioxide being directed for downhole storage (sequestration).

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What is claimed is: 1. A system for the downhole separation of carbon dioxide from natural gas produced from natural gas reservoirs in a formation traversed by a completed well and having a sequestration layer, comprising: a dual reflux pressure swing adsorption (PSA) system with two packed PSA beds contained in PSA tubes located in the well generally maintained at different pressures relative to each other during operation and having top, bottom and middle portions, each middle portion receiving at different times from the formation a mixture of the carbon dioxide and natural gas, wherein said PSA beds generate purified carbon dioxide and purified natural gas from the mixture, the top portions of said PSA beds adapted to receive one at a time some of at least one of said purified natural gas and said purified carbon dioxide, and the bottom portions of said PSA beds adapted to receive one at a time at least some of the other of purified natural gas and purified carbon dioxide; and at least one additional tube adjacent at least one of said PSA tubes for carrying said purified carbon dioxide to the sequestration layer. 2. A system according to claim 1, further comprising: a compressor coupled to said purified carbon dioxide, wherein said compressor compresses said purified carbon dioxide for reinjection into either said top portion or said bottom portion of said packed PSA beds one at a time. 3. A system according to claim 2, wherein: said compressor is located at said surface of said formation. 4. A system according to claim 3, wherein: said mixture is always provided to the higher pressure bed of said PSA beds, and said purified natural gas is taken from said top portions of said PSA beds and said purified carbon dioxide is taken from said bottom portions of said PSA beds. 5. A system according to claim 4, wherein: said PSA beds are adjacent each other and said at least one additional tube comprises at least two additional tubes adjacent said PSA beds, a first of said two additional tubes taking said purified carbon dioxide from said bottom portion of said PSA bed and bringing it to said compressor, and a second of said two tubes taking said purified carbon dioxide from said compressor to the bottom portion of the PSA bed receiving the purified natural gas. 6. A system according to claim 5, further comprising: a plurality of packers through which said PSA tubes and said at least two additional tubes extends. 7. A system according to claim 6, further comprising: a plurality of valves coupled to said PSA tubes and to said at least two additional tubes. 8. A system according to claim 7, wherein: said plurality of valves includes a first valve coupled to said middle portion of said first of said PSA tubes and a second valve coupled to said middle portion of said second of said PSA tubes, said first valve and said second valve respectively coupling said middle portions of said PSA tubes to the mixture of the carbon dioxide and natural gas of the formation. 9. A system according to claim 8, wherein: said plurality of valves includes a third valve coupled to said bottom portion of a first of said PSA tubes, and a fourth valve coupled to said bottom portion of a second of said PSA tubes, said third and fourth valves placing said PSA tubes in communication with said first of said at least two additional tubes for transferring purified carbon dioxide from said PSA beds to said first of said at least two additional tubes. 10. A system according to claim 9, wherein: said plurality of valves includes a fifth valve coupled to a bottom portion of said first of said PSA beds and a sixth valve coupled to a bottom portion of said second of said PSA beds, wherein said second of said at least two additional tubes is in communication with said fifth valve and said sixth valve for transferring compressed purified carbon dioxide to said bottom portions of said PSA beds. 11. A system according to claim 10, wherein: a first and a second of said plurality of packers straddle said first valve and said second valve, and a third and a fourth of said plurality of packers straddle either said third and fourth valves or said fifth and sixth valves. 12. A system according to claim 3, wherein: said mixture is always provided to the higher pressure bed of said PSA beds, said purified natural gas is taken from said bottom portions of said PSA beds and said purified carbon dioxide is taken from said top portions of said PSA beds, said PSA tubes are concentric, said at least one additional tube for carrying said purified carbon dioxide is concentric with said PSA tubes, and said system further comprises a second additional tube concentric with said PSA tubes and said at least one additional tube, said second additional tube for carrying purified natural gas from said bottom portions of said PSA beds to a surface of the formation. 13. A system according to claim 12, further comprising: a packer located at the sequestration layer. 14. A system according to claim 2, wherein: said mixture is always provided to the lower pressure bed of said PSA beds, said purified natural gas is taken from said top portions of said PSA beds and said purified carbon dioxide is taken from said bottom portions of said PSA beds, said PSA tubes are concentric, said at least one additional tube for carrying said purified carbon dioxide is concentric with said PSA tubes, and said at least one additional tube includes a packer located at the sequestration layer. 15. A system according to claim 14, wherein: said compressor is located in the completed well. 16. A system for the production, through a completed well traversing a formation, of natural gas from a production layer in the formation containing natural gas and carbon dioxide, and for sequestration of the carbon dioxide into a sequestration layer in the formation comprising: at least three substantially parallel tubes located in the well, said at least three substantially parallel tubes including two packed pressure swing adsorption (PSA) beds and at least one tube for purified compressed carbon dioxide; a compressor coupled to said at least one tube for purified compressed carbon dioxide and to said PSA beds; a plurality of valves at least some of which are located in the completed well, a first of said valves coupled to a middle portion of a first of said PSA beds and to the production layer, a second of said valves coupled to a middle portion of a second of said PSA beds and to the production layer, a third of said valves coupled to a first of said PSA beds and to said compressor, and a fourth of said valves coupled to a second of said PSA beds and to said compressor, wherein at any given time, one of said two PSA beds produces purified natural gas, and the other of said two PSA beds produces purified carbon dioxide; and means associated with said tube for purified compressed carbon dioxide for directing said purified carbon dioxide into the sequestration layer of the formation. 17. A method for separating a mixture of carbon dioxide and natural gas produced from a natural gas reservoir in a formation traversed by a completed well and having a sequestration layer, comprising: providing a dual reflux pressure swing adsorption (PSA) system with two packed PSA beds contained in PSA tubes having top, middle, and bottom portions; locating said two packed PSA tubes and at least one additional tube in the well; maintaining said two packed PSA beds at different pressures relative to each other during operation; providing each middle portion of said PSA beds one at a time with the mixture of the carbon dioxide and natural gas from the reservoir, wherein said PSA beds generate purified carbon dioxide and purified natural gas from the mixture, and providing the top portions of said PSA beds one at a time with some of at least one of said purified natural gas and said purified carbon dioxide, and the bottom portions of said PSA beds one at a time with at least some of the other of purified natural gas and purified carbon dioxide; obtaining said purified natural gas at a surface of the formation; and piping said purified carbon dioxide through said at least one additional tube for sequestration in the sequestration layer. 18. A method according to claim 17, further comprising: compressing at least some of said purified natural gas and providing at least some of the compressed purified natural gas to a higher pressure bed of said two packed PSA beds. 19. A method according to claim 17, wherein: said PSA beds are adjacent each other and said at least one additional tube comprises at least two additional tubes adjacent said PSA beds, a first of said two additional tubes taking said purified carbon dioxide from said bottom portion of said PSA bed and bringing it to a compressor, and a second of said two tubes taking said purified carbon dioxide from the compressor to the bottom portion of the PSA bed receiving the purified natural gas. 20. A method according to claim 17, wherein: said PSA tubes are concentric, and said at least one additional tube for carrying said purified carbon dioxide is concentric with said PSA tubes.

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Downhole separation of carbon dioxide from natural gas produced from natural gas reservoirs

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Downhole separation of carbon dioxide from natural gas produced from natural gas reservoirs

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