KR900004624A - 수소 및 일산화탄소의 동시 생성방법 및 그 장치 - Google Patents

수소 및 일산화탄소의 동시 생성방법 및 그 장치 Download PDF

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KR900004624A
KR900004624A KR1019890013093A KR890013093A KR900004624A KR 900004624 A KR900004624 A KR 900004624A KR 1019890013093 A KR1019890013093 A KR 1019890013093A KR 890013093 A KR890013093 A KR 890013093A KR 900004624 A KR900004624 A KR 900004624A
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carbon monoxide
hydrogen
unit
permeator
ratio
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KR1019890013093A
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고띠에 삐에르
모네로 크리스띠앙
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레르 리뀌드 쏘시에떼 나노뉨 뿌르 레뛰드 에 렉스 쁠로와 따씨옹 데 프로세드 죠르쥬끌로드
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Publication of KR900004624A publication Critical patent/KR900004624A/ko

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Abstract

내용 없음

Description

수소 및 일산화탄소의 동시 생성방법 및 그 장치
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도 및 제2도는 본 발명에 따른 장치의 2개의 변환체를 계통적으로 도시한 것이며,
제3도는 제2도의 Ⅲ대역의 변환체를 도시한 것이다.

Claims (6)

  1. 수소 및 일산화탄소를 함유한 탄화수소 개질 가스와 같은 합성가스가 탄화수소 개질단위(1)에서 산출되는 타입의 예정된 H2/CO비를 지닌 수소 및 일산화탄소의 동시 생성방법에 있어서, 합성가스는 초과의 H2/CO비로서 산출되고, 상기 비는 투과기(4)에서의 투과에 의해 과량의 수소를 배출함으로써 조절되는 것을 특징으로 하는 수소 및 일산화탄소의 동시 생성방법.
  2. 제1항에 있어서, 합성 가스는 장치(2) 및 (3)에서 탈탄화 및 탈수 후 저온 분리 단위(5)에서 나머지 성분의 저온 분리가 실시되며, 투과는 저온 분리의 상부에서 실시되는 것을 특징으로 하는 방법.
  3. 제1항 또는 제2항에 있어서, 합성가스의 일부가 투과되는 것을 특징으로 하는 방법.
  4. 수소 및 일산화탄소를 함유한 탄화수소 개질 가스와 같은 합성 가스 생성단위(1)을 포함하는, 예정된 H2/CO비를 지닌 수소 및 일산화탄소의 동시적 생성 장치에 있어서, 상기 단위(1)의 하부에 과량의 수소를 제거하기 위한 투과기(4)를 포함하는 것을 특징으로 하는 장치.
  5. 제4항에 있어서, 상기 단위(1)의 하부에 합성가스의 탈탄화 또는 탈수를 위한 수단(2,3) 및 탈탄화 및 탈수 수단으로 부터 배출되는 가스를 냉각시키기기 위한 열교환기(6)을 포함하는 저온분리 단위(5)를 포함하며, 상기 투과기(4)는 열 교환기(6)의 상부에 장착됨을 특징으로 하는 장치.
  6. 제4항 또는 제5항에 있어서, 투과기(4)는 흐름조절성의 바이-패스(21)를 구비하는 것을 특징으로 하는 장치.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019890013093A 1988-09-12 1989-09-11 수소 및 일산화탄소의 동시 생성방법 및 그 장치 KR900004624A (ko)

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Application Number Priority Date Filing Date Title
FR8811883A FR2636250B1 (fr) 1988-09-12 1988-09-12 Procede et installation de recuperation d'hydrogene et de monoxyde de carbone
FR88-11883 1988-09-12

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KR900004624A true KR900004624A (ko) 1990-04-12

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EP (1) EP0359629A1 (ko)
KR (1) KR900004624A (ko)
AU (1) AU4123689A (ko)
BR (1) BR8904558A (ko)
CA (1) CA1339975C (ko)
DK (1) DK446289A (ko)
FI (1) FI894283A (ko)
FR (1) FR2636250B1 (ko)
HU (1) HUT52736A (ko)
NO (1) NO893627L (ko)
PT (1) PT91680A (ko)

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US5354547A (en) * 1989-11-14 1994-10-11 Air Products And Chemicals, Inc. Hydrogen recovery by adsorbent membranes
FR2745000A1 (fr) * 1996-02-16 1997-08-22 Air Liquide Procede et installation de production de monoxyde de carbone
FR2780391B1 (fr) 1998-06-26 2000-10-20 Air Liquide Procede de production de monoxyde de carbone
US6161397A (en) * 1998-08-12 2000-12-19 Air Products And Chemicals, Inc. Integrated cryogenic and non-cryogenic gas mixture separation
US6568206B2 (en) 2001-07-18 2003-05-27 Air Products And Chemicals, Inc. Cryogenic hydrogen and carbon monoxide production with membrane permeate expander
FR2838424B1 (fr) * 2002-04-15 2004-05-28 Air Liquide Procede et installation de separation d'un melange d'hydrogene et de monoxyde de carbone
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HUT52736A (en) 1990-08-28
NO893627L (no) 1990-03-13
CA1339975C (fr) 1998-07-28
BR8904558A (pt) 1990-04-24
FR2636250B1 (fr) 1992-01-17
FR2636250A1 (fr) 1990-03-16
AU4123689A (en) 1990-03-15
DK446289D0 (da) 1989-09-11
PT91680A (pt) 1990-03-30
EP0359629A1 (fr) 1990-03-21
FI894283A0 (fi) 1989-09-11
FI894283A (fi) 1990-03-13
NO893627D0 (no) 1989-09-11

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