KR960037098A - 일산화탄소 및 수소를 제조하는 통합된 증기 메탄 개질 방법 - Google Patents
일산화탄소 및 수소를 제조하는 통합된 증기 메탄 개질 방법 Download PDFInfo
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- KR960037098A KR960037098A KR1019960011489A KR19960011489A KR960037098A KR 960037098 A KR960037098 A KR 960037098A KR 1019960011489 A KR1019960011489 A KR 1019960011489A KR 19960011489 A KR19960011489 A KR 19960011489A KR 960037098 A KR960037098 A KR 960037098A
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- Prior art keywords
- hydrogen
- water
- pressure
- reactor
- cleaning fluid
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- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/56—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids
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- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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Abstract
본 발명은 개질 촉매의 존재하에 탄화수소 및 중기를 개질시켜 CO, 이산화탄소 및 수소의 함량이 높은 개질산물을 생성시킴으로써, 거의 순수한 일산화탄소(CO) 산물 및 거의 순수한 수소 산물을 제조하는 방법에 관한 것이다. 상기 개질 산물은 통합된 연속 분리단계들을 거친 후, 그러한 일련의 분리단계들로부터 회수된 폐기 유출물중에 존재하는 이산화 탄소 및 수소를 통합 수착 촉진 반응(SER) 공정에서 CO로 전이시킨다.
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제8도는 증기-메탄 개질로부터의 개질 산물을 통합된 CO-VSA 유니트와 수소 PSA 유니트에서 분리하여 CO 생성물 스트림, 수소 생성물 스트림 및 폐기 가스 스트림을 생성시키는, CO 및 수소를 제조하는 종래기술의 SMR 방법에 대한 개략도, 제9도는 촉매의 존재하에 메탄 및 물을 반응시켜 이산화탄소, 일산화탄소 및 수소를 포함하는 개질 생성물을 형성하는 거의 순수한 CO 스트림 및 거의 순수한 수소 스트림을 제조하는 본 발명의 SMR 방법의 통상적인 실시태양에 대한 개략도이다. SMR 개질산물은 제1반응기로 보내져 그의 순수한 CO 산물 및 CO-고갈 스트림을 생셩하며, 이 CO-스트림은 또다른 분리단계로 거쳐 거의 순수한 수소 생성물 및 수소-고갈 스트림을 생성한다. 수소 고갈 스트림의 일부에 존재하는 CO2는 본원의 흡착 촉진반응(SER) 공정을 사용하여 수소와 반응시킴으로써 총 공정에 따른 부가량의 CO를 생성시킨다.
Claims (9)
- (a) 증기 메탄 개질 촉매의 존재하에, 700℃ 내지 1000℃ 범위내의 온도 및 2 내지 50 기압 범위내의 압력에서 메탄 및 물을 포함하는 공급 원료를 반응시켜 수소, 일산화탄소, 이산화탄소 및 미반응 원료를 포함하는 개질물을 형성시키는 단계; (b) 상기 개질물에서 물을 제거하여 탈수 개질물을 형성하고, 상기 탈수 개질물을 CO 생성물 및 CO-고갈 생성물로 분리시키는 단계; (c) CO-고갈 스트림을 수소 생성물 및 수소-고갈 스트림으로 분리시킨후, 수소-고갈 스트림을 압축시켜 압축된 수소-고갈 스트림을 형성하는 단계; (d) 각 반응기 내에서 사이클로 수행되는 하기 단계 (1)∼(5)에 따라 소정의 서열로 작동하는 다수개의 반응기내에 수소-고갈 스트림을 유입시키는 단계를 포함하는 일산화탄소 생성물 및 수소 생성물의 제조 방법; (1) 흡수체 및 물 가스 전이 촉매의 혼합물이 수용된 제1반응기에서, 이산화탄소 및 수소를 일산화탄소로 전이시키고 흡착제상에 물을 흡착시키며, 단계 (b)의 탈수된 개질물 스트림내로 재순환되는 CO-함량이 높은 스트림을 형성하기에 충분한 반응조건하에 제1압력에서 압축된 수소-고갈 스트림을 반응시키는 단계; (2) 수소, 이산화탄소, 일산화탄소 및 물로 구성된 혼합물을 배출시킴으로써 제1반응기의 압력을 제2압력으로 역류적 탈압시키는 단계; (3) 흡착제에 비해 흡착성이 약한 세정 유체로 제2압력하에 제1반응기를 역류적 세정함으로써 흡착제로부터 물을 탈착시킨 후, 약-흡착성 세정유체, 미반응 원료, 일산화탄소 및 물을 포함하는 혼합물을 배출시키는 단계; (4) 제2압력하에 수소 및 이산화탄소를 함유하지 않은 CO-함량이 높은 세정유체로서 제1반응기를 역류적 세정하여 약-흡착성 세정 유체를 탈착시킨 후, 약-흡착성 세정 유체, 일산화탄소 및 물로 구성된 혼합물을 배출시키는 단계; 및 (5) 제1반응기내에서 또다른 공정의 사이클을 개시하기 전에 CO-함량이 높은 세정 유체로써 제1반응기를 제2압력으로부터 제1압력으로 역류적 압축시키는 단계.
- 제1항에 있어서, (e)단계 (d)(1)의 제1반응기중에 존재하는 수소와 이산화탄소의 비를 조절하기 위해 단계(c)의 수소-고갈 스트림내에 수소 또는 이산화탄소 원료를 유입시키는 단계를 부가로 포함하는 방법.
- 제1항에 있어서, 제1압력하에 약-흡착성 세정 유체로써 제1반응기를 역류적 세정한 후 미반응 원료, 일산화탄소 및 물로 구성된 혼합물을 배출시키는 단계를 단계 (d)(1)과 단계 (d)(2)의 사이에 부가로 포함하는 방법.
- 제1항에 있어서, 흡착제와 촉매의 혼합물이 5 내지 95중량%의 흡착제 및 95 내지 5중량%의 촉매를 포함하는 방법.
- 제1항에 있어서, 제1압력이 2 내지 50기압이고, 제2압력은 0.05 내지 2기압인 방법.
- 제1항에 있어서, 단계 (d)에서의 흡착제가 제올라이트, 알루미나 또는 실리카겔로 구성된 군중에서 선택되고, 약-흡착성 세정 유체는 메탄, 수소, 질소 및 이산화탄소로 구성된 군에서 선택되는 방법.
- 제1항에 있어서, 원료가 물 및 메탄올 1.5 내지 30의 물 대 메탄의 화학량론적 비율로 포함하는 방법.
- 제1항에 있어서, 증기-메탄 개질 촉매가 니켈-알루미나, 니켈-망간 알루미나 및 귀금속 촉매로 구성된 군중에서 선택되는 방법.
- 제1항에 있어서, 물 가스 전이 촉매가 철-크롬 고온 전이 촉매, 구리-아연 옥사이드 저온 전이 촉매 및 구리-아연 옥사이드 중온 전이 촉매로 구성된 군중에서 선택되는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
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US08/419,317 US6303092B1 (en) | 1995-04-10 | 1995-04-10 | Process for operating equilibrium controlled reactions |
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US08/624,149 US6312658B1 (en) | 1995-04-10 | 1996-04-08 | Integrated steam methane reforming process for producing carbon monoxide and hydrogen |
US08/624,149 | 1996-04-08 |
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KR1019960011487A KR960037097A (ko) | 1995-04-10 | 1996-04-10 | 일산화탄소를 제조하기 위한 통합 증기 메탄 개질 방법 |
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KR1019960011489A KR960037098A (ko) | 1995-04-10 | 1996-04-10 | 일산화탄소 및 수소를 제조하는 통합된 증기 메탄 개질 방법 |
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- 1995-04-10 US US08/419,317 patent/US6303092B1/en not_active Expired - Fee Related
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- 1996-04-03 EP EP96105343A patent/EP0737648B1/en not_active Expired - Lifetime
- 1996-04-03 DE DE69609755T patent/DE69609755T2/de not_active Expired - Fee Related
- 1996-04-03 ES ES96105343T patent/ES2152450T3/es not_active Expired - Lifetime
- 1996-04-08 US US08/624,148 patent/US6328945B1/en not_active Expired - Fee Related
- 1996-04-08 KR KR1019960010404A patent/KR960037099A/ko not_active Application Discontinuation
- 1996-04-08 US US08/624,147 patent/US6315973B1/en not_active Expired - Lifetime
- 1996-04-08 US US08/624,149 patent/US6312658B1/en not_active Expired - Fee Related
- 1996-04-10 EP EP00101685A patent/EP1006079B1/en not_active Expired - Lifetime
- 1996-04-10 TW TW085104199A patent/TW305774B/zh active
- 1996-04-10 KR KR1019960011487A patent/KR960037097A/ko not_active Application Discontinuation
- 1996-04-10 DE DE69638176T patent/DE69638176D1/de not_active Expired - Lifetime
- 1996-04-10 KR KR1019960011488A patent/KR960037108A/ko not_active Application Discontinuation
- 1996-04-10 KR KR1019960011489A patent/KR960037098A/ko not_active Application Discontinuation
- 1996-06-26 TW TW085107690A patent/TW325416B/zh active
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KR100499860B1 (ko) * | 2002-08-29 | 2005-07-07 | (주)에너피아 | 고효율 합성가스 제조용 촉매를 이용한 합성가스의 제조공정 |
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DE69638176D1 (de) | 2010-06-10 |
US6328945B1 (en) | 2001-12-11 |
ES2152450T3 (es) | 2001-02-01 |
EP1006079B1 (en) | 2010-04-28 |
US6303092B1 (en) | 2001-10-16 |
TW305774B (ko) | 1997-05-21 |
EP0737648A3 (en) | 1997-08-13 |
US6315973B1 (en) | 2001-11-13 |
EP1006079A1 (en) | 2000-06-07 |
EP0737648A2 (en) | 1996-10-16 |
TW325416B (en) | 1998-01-21 |
KR960037108A (ko) | 1996-11-19 |
EP0737648B1 (en) | 2000-08-16 |
KR960037099A (ko) | 1996-11-19 |
US6312658B1 (en) | 2001-11-06 |
DE69609755T2 (de) | 2000-12-28 |
KR960037097A (ko) | 1996-11-19 |
CA2173423A1 (en) | 1996-10-11 |
DE69609755D1 (de) | 2000-09-21 |
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