ES2075968T3 - Procedimiento para la produccion de metanol en fase liquida en etapas. - Google Patents

Procedimiento para la produccion de metanol en fase liquida en etapas.

Info

Publication number
ES2075968T3
ES2075968T3 ES92102932T ES92102932T ES2075968T3 ES 2075968 T3 ES2075968 T3 ES 2075968T3 ES 92102932 T ES92102932 T ES 92102932T ES 92102932 T ES92102932 T ES 92102932T ES 2075968 T3 ES2075968 T3 ES 2075968T3
Authority
ES
Spain
Prior art keywords
liquid phase
methanol
gas
reactor system
gas turbine
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
ES92102932T
Other languages
English (en)
Inventor
David William Studer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Air Products and Chemicals Inc
Original Assignee
Air Products and Chemicals Inc
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 Air Products and Chemicals Inc filed Critical Air Products and Chemicals Inc
Application granted granted Critical
Publication of ES2075968T3 publication Critical patent/ES2075968T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/1516—Multisteps
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/1516—Multisteps
    • C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • 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
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

SE PRODUCE EL METANOL DE LA SINTESIS DE UN GAS QUE CONTIENE HIDROGENO, MONOXIDO Y DIOXIDO DE CARBONO EN UN SISTEMA DE REACTOR DE FASE LIQUIDA DE DOS ETAPAS. CADA REACTOR ESTA OPERADO EN UNA GAMA DE TEMPERATURA OPTIMA PARA AUMENTAR AL MAXIMO LA PRODUCCION DE METANOL, Y PODRA ALCANZARSE LA CONVERSION DEL PRODUCTO DE HASTA 9.1 MOLECULAS DE METANOL POR 100 MOLECULAS DE GAS SINTETIZADO, UTILIZANDO UN CATALIZADOR RAZONABLE. LA UTILIZACION TOTAL DEL CATALIZADOR SE AUMENTA MEDIANTE TRANSFERENCIA DE CONTRACORRIENTE INTEGRADA. EN UN MODO ALTERNATIVO DE OPERACION, EL SISTEMA DE REACTOR DE FASE LIQUIDA ESTA INTEGRADO CON UN PROCESO DE GENERACION DE POTENCIA DE CICLO COMBINADO DE GASIFICACION DEL CARBON (CCGC) DONDE SE UTILIZA EL GAS DE SINTESIS SIN REACCIONAR COMO COMBUSTIBLE EN UN GENERADOR DE POTENCIA ELECTRICA TRANSMITIDO POR TURBINA DE GAS. LA OPERACION DE CADA UNO DE LOS REACTORES DE FASE LIQUIDA EN LA GAMA DE TEMPERATURA OPTIMA AUMENTA HASTA EL MAXIMO EL CALOR DISPONIBLE DE REACCION QUE SE RECUPERA COMO VAPOR; EL VAPOR SE UTILIZA EN LA COMBUSTION DE LA TURBINA DE GAS O EN LA TURBINA DE VAPOR CCGC. EL METANOL DEL SISTEMA DE REACTOR DE FASE LIQUIDA PODRA UTILIZARSE COMO COMBUSTIBLE DE PRECISION MAXIMA PARA LA TURBINA DE GAS.
ES92102932T 1991-03-01 1992-02-21 Procedimiento para la produccion de metanol en fase liquida en etapas. Expired - Lifetime ES2075968T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/664,178 US5179129A (en) 1991-03-01 1991-03-01 Staged liquid phase methanol process

Publications (1)

Publication Number Publication Date
ES2075968T3 true ES2075968T3 (es) 1995-10-16

Family

ID=24664900

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92102932T Expired - Lifetime ES2075968T3 (es) 1991-03-01 1992-02-21 Procedimiento para la produccion de metanol en fase liquida en etapas.

Country Status (8)

Country Link
US (1) US5179129A (es)
EP (1) EP0501331B1 (es)
JP (1) JPH0597732A (es)
AU (1) AU1131892A (es)
CA (1) CA2061710C (es)
DE (1) DE69202779T2 (es)
DK (1) DK0501331T3 (es)
ES (1) ES2075968T3 (es)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111140359A (zh) * 2019-12-16 2020-05-12 华北电力大学 太阳能驱动煤气化甲醇合成与零排放发电联产系统

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ES2090854T3 (es) * 1992-02-04 1996-10-16 Air Prod & Chem Procedimiento para producir metanol en fase liquida con reciclado rico en co.
US5666800A (en) * 1994-06-14 1997-09-16 Air Products And Chemicals, Inc. Gasification combined cycle power generation process with heat-integrated chemical production
EP0687648B1 (de) * 1994-06-15 1998-09-16 dbb fuel cell engines GmbH Zweistufige Methanol-Reformierung
BR9709857A (pt) * 1996-06-21 2002-05-21 Syntroleum Corp processo e sistema de produção de gás de sìntese
MY118075A (en) * 1996-07-09 2004-08-30 Syntroleum Corp Process for converting gas to liquids
US5806298A (en) * 1996-09-20 1998-09-15 Air Products And Chemicals, Inc. Gas turbine operation with liquid fuel vaporization
WO1999019277A1 (en) 1997-10-10 1999-04-22 Syntroleum Corporation System and method for converting light hydrocarbons to heavier hydrocarbons with separation of water into oxygen and hydrogen
US5882614A (en) * 1998-01-23 1999-03-16 Exxon Research And Engineering Company Very low sulfur gas feeds for sulfur sensitive syngas and hydrocarbon synthesis processes
US6211254B1 (en) 1999-06-07 2001-04-03 John P. Whitney Process for recycling heterogeneous waste
WO2001017936A2 (de) * 1999-09-07 2001-03-15 Krupp Uhde Gmbh Verfahren und anlage zur methanolherstellung
US6723886B2 (en) 1999-11-17 2004-04-20 Conocophillips Company Use of catalytic distillation reactor for methanol synthesis
CA2357527C (en) 2001-10-01 2009-12-01 Technology Convergence Inc. Methanol recycle stream
US6794417B2 (en) 2002-06-19 2004-09-21 Syntroleum Corporation System and method for treatment of water and disposal of contaminants produced by converting lighter hydrocarbons into heavier hydrocarbon
US20060235090A1 (en) * 2002-12-21 2006-10-19 Haldor Topsoe A/S Process for synthesis of methanol
US6881759B2 (en) * 2003-04-07 2005-04-19 Haldor Topsoe A/S Process for the preparation of methanol
GB0418654D0 (en) * 2004-08-20 2004-09-22 Davy Process Techn Ltd Process
US20060149423A1 (en) * 2004-11-10 2006-07-06 Barnicki Scott D Method for satisfying variable power demand
DE102004058759A1 (de) * 2004-11-30 2006-06-01 Vattenfall Europe Generation Ag & Co. Kg Verfahren zur Bereitstellung eines Brennstoffes für die Gasturbine eines IGCC-Kraftwerkes
EP1928984A1 (en) * 2005-08-19 2008-06-11 Varipower Technology PTY Ltd Method for generating power
US20080260631A1 (en) * 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
JP2010173985A (ja) * 2009-01-30 2010-08-12 Jfe Steel Corp 炭化水素系燃料の製造方法および炭化水素系燃料製造設備
US9057032B2 (en) 2009-05-26 2015-06-16 Inentec Inc. High pressure gasifier system using electrically assisted heating
US9150803B2 (en) * 2009-06-09 2015-10-06 Sundrop Fuels, Inc. Systems and methods for biomass grinding and feeding
US8814961B2 (en) 2009-06-09 2014-08-26 Sundrop Fuels, Inc. Various methods and apparatuses for a radiant-heat driven chemical reactor
US9663363B2 (en) 2009-06-09 2017-05-30 Sundrop Fuels, Inc. Various methods and apparatuses for multi-stage synthesis gas generation
WO2011100830A1 (en) * 2010-02-18 2011-08-25 Hatch Ltd. Multi-stage reaction system
DE102010008857A1 (de) * 2010-02-22 2011-08-25 Lurgi GmbH, 60439 Verfahren zur Herstellung von Methanol
CN104193585A (zh) * 2014-08-06 2014-12-10 华南理工大学 一种焦炉气辅助煤气化制甲醇的系统及工艺
JP6548602B2 (ja) * 2016-03-30 2019-07-24 岩谷産業株式会社 水素供給装置及び水素供給方法
JP6548603B2 (ja) * 2016-03-30 2019-07-24 岩谷産業株式会社 水素供給装置及び水素供給方法
JP7134682B2 (ja) * 2018-04-16 2022-09-12 三菱重工業株式会社 メタノール製造方法およびメタノール製造システム
MY205111A (en) * 2018-06-12 2024-10-02 Haldor Topsoe As A process for methanol production using a low-iron catalyst
CA3127050A1 (en) 2019-01-21 2020-07-30 Eni S.P.A. Methanol production process with higher carbon utilization by co2 recycle
WO2020154284A1 (en) 2019-01-21 2020-07-30 Sabic Global Technologies, B.V. Methanol production process
US10744475B1 (en) 2019-02-08 2020-08-18 David O. Trahan Methanol production reactor apparatus and method of operations using homogeneous catalyst
JP7444560B2 (ja) * 2019-08-02 2024-03-06 三菱ケミカル株式会社 アルコールの製造方法及び製造装置
CN115634636B (zh) * 2022-10-26 2024-03-15 西南化工研究设计院有限公司 一种甲醇低压羰基合成醋酸的自动控制系统及方法

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US2852350A (en) * 1952-12-27 1958-09-16 Rheinpreussen Ag Fur Bergbau A Carbon monoxide hydrogenation synthesis reactors
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DE3320227A1 (de) * 1983-06-03 1984-12-06 Kraftwerk Union AG, 4330 Mülheim Kraftwerk mit einer integrierten kohlevergasungsanlage
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111140359A (zh) * 2019-12-16 2020-05-12 华北电力大学 太阳能驱动煤气化甲醇合成与零排放发电联产系统

Also Published As

Publication number Publication date
US5179129A (en) 1993-01-12
EP0501331A2 (en) 1992-09-02
CA2061710C (en) 1999-08-17
DE69202779T2 (de) 1995-10-12
JPH0597732A (ja) 1993-04-20
EP0501331B1 (en) 1995-06-07
CA2061710A1 (en) 1992-09-02
DE69202779D1 (de) 1995-07-13
EP0501331A3 (en) 1992-09-23
DK0501331T3 (da) 1995-07-24
AU1131892A (en) 1992-09-10

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