Method and integrated device for separating air and heating an air gas originating from an air separation device
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
F25J-003/00
F25J-003/04
출원번호
US-0583486
(2011-03-03)
등록번호
US-9360251
(2016-06-07)
우선권정보
FR-10 51676 (2010-03-09)
국제출원번호
PCT/FR2011/050445
(2011-03-03)
§371/§102 date
20120907
(20120907)
국제공개번호
WO2011/110775
(2011-09-15)
발명자
/ 주소
Dubettier-Grenier, Richard
Tranier, Jean-Pierre
출원인 / 주소
L'Air Liquide Société Anonyme Pour L'Étude Et L'Exploitation Des Procedes Georges Claude
대리인 / 주소
Murray, Justin K.
인용정보
피인용 횟수 :
0인용 특허 :
5
초록▼
The invention relates to an integrated device for separating air and heating a gas in the air resulting from said air separation, comprising: an air separation device (9); a heat exchanger (13, 43); a channel for conveying the gas in the air to the heat exchanger; and a channel for conveying water t
The invention relates to an integrated device for separating air and heating a gas in the air resulting from said air separation, comprising: an air separation device (9); a heat exchanger (13, 43); a channel for conveying the gas in the air to the heat exchanger; and a channel for conveying water to the heat exchanger, the water-conveying channel being connected to the water inlet or water outlet of a water preheat exchanger (5) or a water deaerator (27). According to the invention, the preheat exchanger and/or the deaerator are connected to an oxy-combustion boiler (19) in order to convey water to and from the boiler, said boiler also being connected to the separation device in order to receive an oxygen-enriched gas (17).
대표청구항▼
1. An integrated method for separation of air and heating of an air gas produced by separation of air, the method comprising the steps of: compressing air in a compressor:cooling the air in a water preheating exchanger:feeding the air to an air separation device under conditions effective to separat
1. An integrated method for separation of air and heating of an air gas produced by separation of air, the method comprising the steps of: compressing air in a compressor:cooling the air in a water preheating exchanger:feeding the air to an air separation device under conditions effective to separate the air in the air separation device to produce at least an oxygen enriched gas and a nitrogen enriched gas;introducing the oxygen enriched gas from the air separation device to an oxycombustion boiler; andheating either the nitrogen enriched gas or the oxygen enriched gas coming from the air separation device by indirect exchange of heat with liquid water in an air gas heat exchanger, wherein the air gas heat exchanger is in fluid communication with a hot water source selected from the group consisting of the water preheating exchanger, a water de-aerator, and combinations thereof, wherein the water preheating exchanger and the water de-aerator are in fluid communication with the oxycombustion boiler, such that the oxycombustion boiler is configured to receive a hot water stream originating from the deaerator and the water preheating exchanger is configured to receive a cold water stream originating from the oxycombustion boiler. 2. The method as claimed in claim 1, wherein the liquid water used to heat either the oxygen enriched gas or the nitrogen enriched gas has been heated in the water preheating exchanger or de-aerated in the de-aerator. 3. The method as claimed in claim 1, further comprising the step of purifying the air in an air purifier before feeding the air to the air separation device. 4. The method as claimed in claim 3, further comprising the step of regenerating the air purifier using the heated nitrogen enriched gas coming from the air gas heat exchanger. 5. The method as claimed in claim 1, wherein all of the air compressed in the compressor is sent to the air separation device. 6. The method as claimed in claim 1, wherein the water cooled in the air gas heat exchanger is sent back to the water preheating exchanger to preheat the water. 7. The method as claimed in claim 1, wherein the liquid water sent to the heat exchanger is at a pressure between 5 and 20 bar absolute. 8. An integrated device for separating air and heating an air gas resulting from said air separation, the integrated device comprising: an air separation device configured to receive a pressurized air stream and separate the pressurized air stream into an oxygen stream and a nitrogen stream;an oxycombustion boiler configured to receive the oxygen stream from the air separation device and a hot water stream, wherein the oxycombustion boiler produces a cooled water stream;an air gas heat exchanger in fluid communication with the air separation unit, such that the air gas heat exchanger is an indirect heat exchanger and is configured to heat the air gas against liquid water, wherein the air gas is selected from the group consisting of nitrogen, oxygen, and combinations thereof;a water pre-heating exchanger in fluid communication with a water outlet of the oxycombustion boiler, wherein the water pre-heating exchanger is configured to heat the cooled water stream from the water outlet of the oxycombustion boiler against the pressurized air stream to produce the hot water stream; anda water circuit comprising a water compressor, the water pre-heating exchanger, the air gas heat exchanger, and the water outlet of the oxycombustion boiler, wherein the water circuit is configured to: receive the cooled water stream from the water outlet of the oxycombustion boiler and transfer the cooled water to the water compressor for compression of the cooled water stream,transfer the cooled water stream to the water pre-heating exchanger for indirect heat exchange against the pressurized air stream to form a hot water stream,transfer the hot water stream to the air gas heat exchanger for indirect heat exchange against the air gas stream to produce a cold water recycle stream, andtransfer the cold water recycle stream to a point upstream the water compressor and downstream the water outlet of the oxycombustion boiler. 9. The integrated device as claimed in claim 8, wherein the water circuit further comprises a de-aerator in fluid communication with the air gas heat exchanger, the water pre-heating exchanger, and a water inlet of the oxycombustion boiler, wherein the de-aerator is configured to receive at least a portion of the hot water stream and remove dissolved gas within the hot water stream. 10. The integrated device as claimed in claim 9, wherein the air gas heat exchanger is configured to receive the hot water stream from the deaerator. 11. The integrated device as claimed in claim 8, wherein the air gas heated in the air gas heat exchanger is oxygen. 12. The integrated device as claimed in claim 8, wherein the cooled water stream, the hot water stream, and the cold water recycle stream are all in liquid form. 13. An integrated method for separation of air and heating of an air gas produced by separation of air, the method comprising the steps of: compressing air in a compressor;cooling the air in a water preheating exchanger;feeding the air to an air separation device under conditions effective to separate the air in the air separation device to produce at least an oxygen enriched gas and a nitrogen enriched gas;introducing the oxygen enriched gas from the air separation device to an oxycombustion boiler; andheating the oxygen enriched gas coming from the air separation device by indirect exchange of heat with a hot water stream in an air gas heat exchanger, wherein the air gas heat exchanger is in fluid communication with a hot water outlet of a water de-aerator, wherein an inlet of the water preheating exchanger and the hot water outlet of the water de-aerator are in fluid communication with the oxycombustion boiler, such that the oxycombustion boiler is configured to receive a hot water stream originating from the deaerator, the water preheating exchanger is configured to receive a cold water stream originating from the oxycombustion boiler, and the air gas heat exchanger is configured to receive the hot water stream originating from the deaerator. 14. The integrated device as claimed in claim 13, wherein the hot water stream from the deaerator is in liquid form.
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이 특허에 인용된 특허 (5)
Marin Ovidiu ; Charon Olivier ; Ha Bao, Integrated air separation process.
Hata Yuichi (Tokyo JPX) Sasaki Jun (Kanagawa JPX) Kawamura Mamoru (Mie JPX) Nakamura Maki (Kanagawa JPX) Taki Kazuya (Kanagawa JPX) Okada Shuichi (Kanagawa JPX), Process for producing various gases for semiconductor production factories.
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