BRPI0900944A2 - processo para a produção de hidrogênio altamente integrado de modo térmico reformando-se uma matéria-prima de hidrocarboneto - Google Patents

processo para a produção de hidrogênio altamente integrado de modo térmico reformando-se uma matéria-prima de hidrocarboneto

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Publication number
BRPI0900944A2
BRPI0900944A2 BRPI0900944-2A BRPI0900944A BRPI0900944A2 BR PI0900944 A2 BRPI0900944 A2 BR PI0900944A2 BR PI0900944 A BRPI0900944 A BR PI0900944A BR PI0900944 A2 BRPI0900944 A2 BR PI0900944A2
Authority
BR
Brazil
Prior art keywords
reforming
stage
hydrocarbon feedstock
production
integrated hydrogen
Prior art date
Application number
BRPI0900944-2A
Other languages
English (en)
Inventor
Fabrice Giroudiere
Christophe Boyer
Original Assignee
Inst Francais Du Petrole
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Application filed by Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of BRPI0900944A2 publication Critical patent/BRPI0900944A2/pt
Publication of BRPI0900944B1 publication Critical patent/BRPI0900944B1/pt

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    • 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
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/323—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
    • C—CHEMISTRY; METALLURGY
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    • 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
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/382—Multi-step processes
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    • 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
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/48—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
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    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • 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
    • C—CHEMISTRY; METALLURGY
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    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C—CHEMISTRY; METALLURGY
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    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
    • C—CHEMISTRY; METALLURGY
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    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
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    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465—Composition of the impurity
    • C01B2203/047—Composition of the impurity the impurity being carbon monoxide
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    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
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    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1217—Alcohols
    • C01B2203/1229—Ethanol
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    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
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    • C01B2203/1258—Pre-treatment of the feed
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    • C01B2203/1288—Evaporation of one or more of the different feed components
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    • C01B2203/14—Details of the flowsheet
    • C01B2203/148—Details of the flowsheet involving a recycle stream to the feed of the process for making hydrogen or synthesis gas
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    • C01B2203/16—Controlling the process
    • C01B2203/1614—Controlling the temperature
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    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

PROCESSO PARA A PRODUçãO DE HIDROGêNIO ALTAMENTE INTEGRADO DE MODO TéRMICO REFORMANDO-SE UMA MATéRIA-PRIMA DE HIDROCARBONETO. A presente invenção refere-se a um processo para a produção de hidrogênio altamente integrado de modo térmico reformando-se uma matéria-prima de hidrocarboneto que compreende um estágio a em que uma corrente de ar ou água, cuja temperatura é menor em pelo menos 200°C do que a temperatura de combustão dentro de um queimador, é misturada com o efluente que é obtido do dito queimador, de modo a reduzir a temperatura deste efluente para menos do que 725°C; um estágio b em que a mistura que é obtida do estágio a entra em um primeiro trocador de calor e é usada para superaquecer pelo menos uma corrente de vapor d'água e/ou matéria-prima de hidrocarboneto na forma gasosa, por meio do qual a dita corrente que é assim superaquecida por troca de calor indireta é injetada diretamente em um reator de reformação onde ela é usada como um combustível; e um estágio c em que a mistura que é obtida do estágio b entra em um segundo trocador de calor e é usada para evaporar totalmente uma corrente de água líquida e/ou matéria-prima de hidrocarboneto.
BRPI0900944-2A 2008-03-28 2009-03-23 Processo para a produção de hidrogênio altamente integrado de modo térmico reformando-se uma matéria-prima de hidrocarboneto BRPI0900944B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/057,591 US8894967B2 (en) 2008-03-28 2008-03-28 Process for the production of highly thermally-integrated hydrogen by reforming a hydrocarbon feedstock
US12/057,591 2008-03-28

Publications (2)

Publication Number Publication Date
BRPI0900944A2 true BRPI0900944A2 (pt) 2009-12-01
BRPI0900944B1 BRPI0900944B1 (pt) 2019-05-21

Family

ID=40674195

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0900944-2A BRPI0900944B1 (pt) 2008-03-28 2009-03-23 Processo para a produção de hidrogênio altamente integrado de modo térmico reformando-se uma matéria-prima de hidrocarboneto

Country Status (7)

Country Link
US (1) US8894967B2 (pt)
EP (1) EP2107043B1 (pt)
CN (1) CN101544353A (pt)
BR (1) BRPI0900944B1 (pt)
CA (1) CA2659547C (pt)
ES (1) ES2388210T3 (pt)
MY (1) MY149496A (pt)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2960450B1 (fr) 2010-05-25 2013-02-22 Inst Francais Du Petrole Procede de production anaerobie d'hydrogene
FR2969593B1 (fr) 2010-12-22 2014-08-29 IFP Energies Nouvelles Amelioration d'un procede de production d'hydrogene integre thermiquement par reformage d'une charge hydrocarbonee
FR2995601B1 (fr) 2012-09-20 2016-05-27 Ifp Energies Now Procede de production d'hydrogene pur a partir d'une charge hydrocarbonee denaturee incluant une etape de desulfuration avec controle de temperature ameliore en amont du psa
RU2614668C1 (ru) * 2016-05-20 2017-03-28 Андрей Владиславович Курочкин Водородная установка
KR101881973B1 (ko) * 2016-12-05 2018-07-25 주식회사 포스코 수소 생산 설비 및 수소 생산 방법
CN108408689B (zh) * 2018-05-30 2021-08-17 大连大学 一种无水制氢系统
CN114408862A (zh) * 2022-01-26 2022-04-29 中国科学院生态环境研究中心 一种中小型生物乙醇重整制氢的装置系统及重整制氢的方法

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GB1540444A (en) * 1976-05-06 1979-02-14 Jetaire Co Ltd Heaters
DE10010071C2 (de) * 2000-03-02 2002-04-25 Xcellsis Gmbh Gaserzeugungsvorrichtung und Verfahren zum Starten derselben
US6835354B2 (en) * 2000-04-05 2004-12-28 Hyradix, Inc. Integrated reactor
AU7228101A (en) * 2000-07-10 2002-01-21 Global Thermoelectric Inc Integrated module for solid oxide fuel cell systems
EP1349647A4 (en) * 2000-12-12 2006-11-08 Texaco Development Corp DOUBLE-STACK COMPACT FUEL PROCESSING DEVICE FOR GENERATING A HYDROGEN-RICH GAS
CA2446333A1 (en) 2001-05-02 2002-11-07 Hydrogen Burner Technology, Inc. Hydrogen generation
JP3778038B2 (ja) * 2001-09-19 2006-05-24 日産自動車株式会社 燃料改質システム
FR2867464B1 (fr) * 2004-03-10 2006-06-09 Inst Francais Du Petrole Procede de production d'hydrogene a tres haute purete a partir d'alcools comportant au moins deux atomes de carbone
EP1750836A4 (en) 2004-05-28 2008-04-02 Hyradix Inc METHOD FOR PRODUCING HYDROGEN BY PARTIAL OXIDATION / STEAM REFORMING
US7964176B2 (en) * 2005-03-29 2011-06-21 Chevron U.S.A. Inc. Process and apparatus for thermally integrated hydrogen generation system
KR100718116B1 (ko) * 2006-05-15 2007-05-15 삼성에스디아이 주식회사 고온용 ｐｅｍ 연료전지 시스템

Also Published As

Publication number Publication date
US20090241418A1 (en) 2009-10-01
CA2659547A1 (fr) 2009-09-28
MY149496A (en) 2013-09-13
EP2107043A1 (fr) 2009-10-07
US8894967B2 (en) 2014-11-25
CA2659547C (fr) 2016-07-12
EP2107043B1 (fr) 2012-05-16
BRPI0900944B1 (pt) 2019-05-21
ES2388210T3 (es) 2012-10-10
CN101544353A (zh) 2009-09-30

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