EA200501128A1 - Установка для конверсии замещением и способ управления установкой - Google Patents

Установка для конверсии замещением и способ управления установкой

Info

Publication number
EA200501128A1
EA200501128A1 EA200501128A EA200501128A EA200501128A1 EA 200501128 A1 EA200501128 A1 EA 200501128A1 EA 200501128 A EA200501128 A EA 200501128A EA 200501128 A EA200501128 A EA 200501128A EA 200501128 A1 EA200501128 A1 EA 200501128A1
Authority
EA
Eurasian Patent Office
Prior art keywords
installation
gas
substitution
management
replacement reactor
Prior art date
Application number
EA200501128A
Other languages
English (en)
Other versions
EA007305B1 (ru
Inventor
Эшок Рао
Кит Стролер
Original Assignee
Флуор Корпорейшн
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Флуор Корпорейшн filed Critical Флуор Корпорейшн
Publication of EA200501128A1 publication Critical patent/EA200501128A1/ru
Publication of EA007305B1 publication Critical patent/EA007305B1/ru

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
    • C10K3/04—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment reducing the carbon monoxide content, e.g. water-gas shift [WGS]
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C01B2203/0288—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step containing two CO-shift steps

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Industrial Gases (AREA)

Abstract

Согласно изобретению значительная часть пара при получении водорода из синтез-газа (и из других газов со сравнительно высоким отношением CO к H) используется для управления температурой в реакторах замещения. Поэтому считается, что полное потребление пара может быть существенно снижено разделением питающего потока газа на первую и вторую части, при этом первую часть газа подают в первый реактор замещения для формирования продукта, который затем соединяют со второй частью газа перед их вводом во второй реактор замещения.Отчет о международном поиске был опубликован 2004.12.02.
EA200501128A 2003-01-13 2004-01-13 Установка для конверсии замещением и способ управления установкой EA007305B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US43991203P 2003-01-13 2003-01-13
PCT/US2004/000926 WO2004062764A2 (en) 2003-01-13 2004-01-13 Improved configuration and process for shift conversion

Publications (2)

Publication Number Publication Date
EA200501128A1 true EA200501128A1 (ru) 2005-12-29
EA007305B1 EA007305B1 (ru) 2006-08-25

Family

ID=32713522

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200501128A EA007305B1 (ru) 2003-01-13 2004-01-13 Установка для конверсии замещением и способ управления установкой

Country Status (10)

Country Link
US (1) US20060236697A1 (ru)
EP (1) EP1597341B1 (ru)
JP (1) JP4473223B2 (ru)
CN (1) CN100393854C (ru)
AU (1) AU2004204831B2 (ru)
CA (1) CA2513212C (ru)
EA (1) EA007305B1 (ru)
MX (1) MXPA05007545A (ru)
WO (1) WO2004062764A2 (ru)
ZA (1) ZA200505702B (ru)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101094910A (zh) * 2004-12-30 2007-12-26 国际壳牌研究有限公司 有关煤变为液体的方法的改进
US7510696B2 (en) 2005-02-07 2009-03-31 Air Products And Chemicals, Inc. Method and apparatus for the production of hydrogen-rich gas
DE102006032104A1 (de) * 2006-07-11 2008-01-24 Linde Ag Verfahren zur Erzeugung von Wasserstoff und Wasserstoff enthaltenden Gasgemischen
DE102007059243A1 (de) * 2007-12-07 2009-06-10 Uhde Gmbh Verfahren zur Entschwefelung olefinhaltiger Einsatzstoffe
JP5529413B2 (ja) 2008-12-12 2014-06-25 三菱重工業株式会社 水素製造システムおよび発電システム
US7789945B2 (en) * 2009-09-25 2010-09-07 Uop Llc Maintaining low carbon monoxide levels in product carbon dioxide
US8211213B2 (en) * 2009-12-07 2012-07-03 Uop Llc Maintaining lowered CO in a CO2 product stream in a process for treating synthesis gas
JP5495749B2 (ja) * 2009-12-10 2014-05-21 三菱重工業株式会社 水素製造設備および発電プラント
CN102002403B (zh) * 2010-11-09 2013-06-19 中国石油化工股份有限公司 一种低水气比串中水气比的co变换工艺
KR102472112B1 (ko) * 2014-10-24 2022-11-28 리써치 트라이앵글 인스티튜트 가스 스트림으로부터 산 가스를 제거하기 위한 통합 시스템 및 방법
US10549991B2 (en) 2015-02-27 2020-02-04 Haldor Topsøe A/S4 Method for production of a hydrogen rich gas

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3904389A (en) * 1974-08-13 1975-09-09 David L Banquy Process for the production of high BTU methane-containing gas
JPS5382690A (en) * 1976-12-29 1978-07-21 Chiyoda Chem Eng & Constr Co Ltd Improved preparation of synthetic gas for ammonia
DE2709768A1 (de) * 1977-03-07 1978-09-21 Metallgesellschaft Ag Verfahren zum katalytischen konvertieren von rohgas aus der vergasung fester brennstoffe
US4159236A (en) * 1978-05-12 1979-06-26 Gulf Oil Corporation Method for combining coal liquefaction and gasification processes
US4383837A (en) * 1979-12-28 1983-05-17 Atlantic Richfield Company Efficient methane production with metal hydrides
US4863707A (en) * 1982-09-30 1989-09-05 Engelhard Corporation Method of ammonia production
US4476683A (en) * 1982-12-20 1984-10-16 General Electric Company Energy efficient multi-stage water gas shift reaction
CA1229485A (en) * 1984-01-23 1987-11-24 Toyo Engineering Corporation Process for refining an ammonia synthesis gas
US4592860A (en) * 1984-02-07 1986-06-03 Union Carbide Corporation Process and apparatus for ammonia synthesis gas production
JPH07133101A (ja) * 1993-11-01 1995-05-23 Aqueous Res:Kk 燃料改質装置
DE10061084A1 (de) * 2000-12-08 2002-07-04 Emitec Emissionstechnologie Reformeranlage mit Wärmeschild

Also Published As

Publication number Publication date
AU2004204831A1 (en) 2004-07-29
CA2513212A1 (en) 2004-07-29
WO2004062764A2 (en) 2004-07-29
WO2004062764A3 (en) 2004-12-02
ZA200505702B (en) 2006-04-26
CN1759164A (zh) 2006-04-12
CA2513212C (en) 2009-03-17
CN100393854C (zh) 2008-06-11
AU2004204831B2 (en) 2008-09-11
EP1597341B1 (en) 2015-06-03
EP1597341A4 (en) 2012-03-07
EP1597341A2 (en) 2005-11-23
EA007305B1 (ru) 2006-08-25
JP2006513128A (ja) 2006-04-20
JP4473223B2 (ja) 2010-06-02
US20060236697A1 (en) 2006-10-26
MXPA05007545A (es) 2005-09-21

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Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ BY KZ KG MD TJ TM

MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): RU