ES2111190T3 - Procedimiento integrado de produccion de gas combustible y de compuestos organicos oxigenados a partir del gas de sintesis. - Google Patents

Procedimiento integrado de produccion de gas combustible y de compuestos organicos oxigenados a partir del gas de sintesis.

Info

Publication number
ES2111190T3
ES2111190T3 ES94101419T ES94101419T ES2111190T3 ES 2111190 T3 ES2111190 T3 ES 2111190T3 ES 94101419 T ES94101419 T ES 94101419T ES 94101419 T ES94101419 T ES 94101419T ES 2111190 T3 ES2111190 T3 ES 2111190T3
Authority
ES
Spain
Prior art keywords
gas
liquid
synthesis gas
product
regenerated
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
ES94101419T
Other languages
English (en)
Inventor
Robert Byron Moore
William Patrick Hegarty
David William Studer
Edward John Tirados
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 ES2111190T3 publication Critical patent/ES2111190T3/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
    • C07C27/00—Processes involving the simultaneous production of more than one class of oxygen-containing compounds
    • C07C27/04—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by reduction of oxygen-containing compounds
    • C07C27/06—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by reduction of oxygen-containing compounds by hydrogenation of oxides of carbon
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Industrial Gases (AREA)

Abstract

UN PRODUCTO LIQUIDO ORGANICO OXIGENADO Y UN GAS COMBUSTIBLE SE PRODUCEN A PARTIR DE UNA PARTE DE GAS DE SINTESIS QUE COMPRENDE HIDROGENO, MONOXIDO DE CARBONO, DIOXIDO DE CARBONO Y COMPUESTOS CON CONTENIDO DE AZUFRE EN UN TRATAMIENTO DE SUMINISTRO INTEGRADO Y UN SISTEMA DE REACCION CATALITICA. PARA EVITAR EL ENVENENAMIENTO DE CATALIZADOR, LOS COMPUESTOS QUE CONTIENEN AZUFRE EN EL SUMINISTRO DEL REACTOR SON ABSORBIDOS EN UN LIQUIDO QUE COMPRENDE EL PRODUCTO DEL REACTOR, Y EL LIQUIDO CON CONTENIDO DE AZUFRE RESULTANTE SE REGENERA CON GAS DE SINTESIS NO TRATADO DEL REACTOR. EL GAS REGENERADO SE COMBINA CON EL GAS DE SINTESIS RESTANTE PARA SUMINISTRAR UN PRODUCTO DE GAS COMBUSTIBLE. UNA PARTE DEL LIQUIDO REGENERADO SE UTILIZA PARA RECOMPONER EL ABSORBEDOR Y EL RESTO ES EXTRAIDO COMO UN PRODUCTO LIQUIDO. EL METODO ES PARTICULARMENTE UTIL PARA LA INTEGRACION CON UN SISTEMA DE GASIFICACION DE CARBON DE CICLO COMBINADO QUE UTILICE UNA TURBINA DE GAS PARA LA GENERACION DE ENERGIA ELECTRICA.
ES94101419T 1993-02-01 1994-01-31 Procedimiento integrado de produccion de gas combustible y de compuestos organicos oxigenados a partir del gas de sintesis. Expired - Lifetime ES2111190T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/012,092 US5392594A (en) 1993-02-01 1993-02-01 Integrated production of fuel gas and oxygenated organic compounds from synthesis gas

Publications (1)

Publication Number Publication Date
ES2111190T3 true ES2111190T3 (es) 1998-03-01

Family

ID=21753359

Family Applications (1)

Application Number Title Priority Date Filing Date
ES94101419T Expired - Lifetime ES2111190T3 (es) 1993-02-01 1994-01-31 Procedimiento integrado de produccion de gas combustible y de compuestos organicos oxigenados a partir del gas de sintesis.

Country Status (6)

Country Link
US (1) US5392594A (es)
EP (1) EP0609813B1 (es)
CA (1) CA2114205C (es)
DE (1) DE69406559T2 (es)
DK (1) DK0609813T3 (es)
ES (1) ES2111190T3 (es)

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US5912986A (en) * 1994-06-21 1999-06-15 Eastman Kodak Company Evidential confidence measure and rejection technique for use in a neural network based optical character recognition system
US6324827B1 (en) 1997-07-01 2001-12-04 Bp Corporation North America Inc. Method of generating power in a dry low NOx combustion system
US7962408B2 (en) * 1999-11-05 2011-06-14 American Express Travel Related Services Company, Inc. Systems and methods for establishing an allocation of an amount between transaction accounts
CA2357527C (en) 2001-10-01 2009-12-01 Technology Convergence Inc. Methanol recycle stream
US6602324B2 (en) 2001-11-15 2003-08-05 Air Products And Chemicals, Inc. Sulfur control in ion-conducting membrane systems
US6887907B2 (en) * 2003-03-05 2005-05-03 L'air Liquide - Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Process and apparatus for the production of dimethyl ether
US7229587B2 (en) * 2003-04-03 2007-06-12 Custom - Pak, Inc. Blow molded container having holes therein and method and apparatus for facilitating the creation thereof
US20060149423A1 (en) * 2004-11-10 2006-07-06 Barnicki Scott D Method for satisfying variable power demand
US20060096298A1 (en) * 2004-11-10 2006-05-11 Barnicki Scott D Method for satisfying variable power demand
NO20051895D0 (no) * 2005-04-19 2005-04-19 Statoil Asa Fremgangsmate for produksjon av elektrisk energi og CO2 fra et hydrokarbon rastoff
US7690204B2 (en) * 2005-10-12 2010-04-06 Praxair Technology, Inc. Method of maintaining a fuel Wobbe index in an IGCC installation
US7722690B2 (en) * 2006-09-29 2010-05-25 Kellogg Brown & Root Llc Methods for producing synthesis gas
US8888875B2 (en) * 2006-12-28 2014-11-18 Kellogg Brown & Root Llc Methods for feedstock pretreatment and transport to gasification
US7879119B2 (en) * 2007-07-20 2011-02-01 Kellogg Brown & Root Llc Heat integration and condensate treatment in a shift feed gas saturator
GB0715101D0 (en) * 2007-08-03 2007-09-12 Johnson Matthey Plc Process
US8221513B2 (en) * 2008-01-29 2012-07-17 Kellogg Brown & Root Llc Low oxygen carrier fluid with heating value for feed to transport gasification
US9132401B2 (en) 2008-07-16 2015-09-15 Kellog Brown & Root Llc Systems and methods for producing substitute natural gas
US7955403B2 (en) * 2008-07-16 2011-06-07 Kellogg Brown & Root Llc Systems and methods for producing substitute natural gas
US9157043B2 (en) 2008-07-16 2015-10-13 Kellogg Brown & Root Llc Systems and methods for producing substitute natural gas
US9157042B2 (en) 2008-07-16 2015-10-13 Kellogg Brown & Root Llc Systems and methods for producing substitute natural gas
US8017539B2 (en) * 2008-10-22 2011-09-13 Uop Llc Once through regeneration for an olefin cracking reactor
US20100132257A1 (en) * 2008-12-01 2010-06-03 Kellogg Brown & Root Llc Systems and Methods for Increasing Carbon Dioxide in Gasification
US9133405B2 (en) 2010-12-30 2015-09-15 Kellogg Brown & Root Llc Systems and methods for gasifying a feedstock
DE102012110520B4 (de) * 2012-11-02 2019-01-31 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Verfahren zur Herstellung von trockenem synthetischem Erdgas (SNG)
DE102014209924A1 (de) * 2014-05-23 2015-11-26 Matthias Enzenhofer Vorrichtung und Verfahren zur Behandlung eines Gasstroms
WO2018004993A1 (en) 2016-07-01 2018-01-04 Res Usa, Llc Reduction of greenhouse gas emission
US9981896B2 (en) 2016-07-01 2018-05-29 Res Usa, Llc Conversion of methane to dimethyl ether
WO2018004994A1 (en) 2016-07-01 2018-01-04 Res Usa, Llc Fluidized bed membrane reactor

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Publication number Priority date Publication date Assignee Title
US2863527A (en) * 1949-09-15 1958-12-09 Metallgesellschaft Ag Process for the purification of gases
DE956225C (de) * 1951-06-03 1957-02-14 Metallgesellschaft Ag Verfahren zur Erzeugung eines fuer Stadt- oder Ferngaszwecke geeigneten Brenngases
US3718006A (en) * 1968-12-11 1973-02-27 Linde Ag Process for selective absorption
US4031123A (en) * 1975-11-21 1977-06-21 Chem Systems Inc. Methanol production in a paraffinic medium
US4277416A (en) * 1977-02-17 1981-07-07 Aminoil, Usa, Inc. Process for producing methanol
ATE3536T1 (de) * 1980-02-12 1983-06-15 Chem Systems, Inc. Verfahren zur herstellung von methanol.
US4341069A (en) * 1980-04-02 1982-07-27 Mobil Oil Corporation Method for generating power upon demand
DE3319732A1 (de) * 1983-05-31 1984-12-06 Kraftwerk Union AG, 4330 Mülheim Mittellastkraftwerk mit integrierter kohlevergasungsanlage zur erzeugung von strom und methanol
DE3320227A1 (de) * 1983-06-03 1984-12-06 Kraftwerk Union AG, 4330 Mülheim Kraftwerk mit einer integrierten kohlevergasungsanlage
DE3343916A1 (de) * 1983-12-05 1985-06-13 Linde Ag, 6200 Wiesbaden Verfahren und vorrichtung zum regenerieren eines loesungsmittels
US4524581A (en) * 1984-04-10 1985-06-25 The Halcon Sd Group, Inc. Method for the production of variable amounts of power from syngas
US4765132A (en) * 1985-03-19 1988-08-23 General Electric Company Process for combustion of a fuel containing sulfur through the use of a gas turbine
US4824869A (en) * 1988-02-22 1989-04-25 Texaco Inc. Base-modified metal oxide catalysts for the conversion of synthesis gas to alcohols
US4946477A (en) * 1988-04-07 1990-08-07 Air Products And Chemicals, Inc. IGCC process with combined methanol synthesis/water gas shift for methanol and electrical power production
EP0353920A3 (en) * 1988-08-01 1991-08-28 Texaco Development Corporation Slurry-phase process to increase yield of mixed alcohols from synthesis gas
US4957515A (en) * 1988-11-03 1990-09-18 Air Products And Chemicals, Inc. Process for sulfur removal and recovery from fuel gas using physical solvent

Also Published As

Publication number Publication date
CA2114205A1 (en) 1994-08-02
DK0609813T3 (da) 1998-03-30
EP0609813A1 (en) 1994-08-10
DE69406559T2 (de) 1998-03-05
EP0609813B1 (en) 1997-11-05
DE69406559D1 (de) 1997-12-11
US5392594A (en) 1995-02-28
CA2114205C (en) 1999-05-11

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