CL2004000742A1 - Proceso para preparar ch3oh con un gas de sintesis que contiene co2, el gas reacciona en condiciones de condensacion de ch2oh, el reactor contiene particulas de catalizador suspendidas en ch2oh y agua, y la corriente reciclada comprende al menos uno - Google Patents

Proceso para preparar ch3oh con un gas de sintesis que contiene co2, el gas reacciona en condiciones de condensacion de ch2oh, el reactor contiene particulas de catalizador suspendidas en ch2oh y agua, y la corriente reciclada comprende al menos uno

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Publication number
CL2004000742A1
CL2004000742A1 CL200400742A CL2004000742A CL2004000742A1 CL 2004000742 A1 CL2004000742 A1 CL 2004000742A1 CL 200400742 A CL200400742 A CL 200400742A CL 2004000742 A CL2004000742 A CL 2004000742A CL 2004000742 A1 CL2004000742 A1 CL 2004000742A1
Authority
CL
Chile
Prior art keywords
methanol
ch2oh
suspended
condensation
conditions
Prior art date
Application number
CL200400742A
Other languages
English (en)
Inventor
Erik Kojlund Nielsen Ceci Poul
Original Assignee
Haldor Topsoe As
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 Haldor Topsoe As filed Critical Haldor Topsoe As
Publication of CL2004000742A1 publication Critical patent/CL2004000742A1/es

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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
    • C07C29/1512—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 characterised by reaction conditions
    • 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)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

LA PRESENTE INVENCION CONSISTE, EN UN NOVEDOSO PROCESO PARA LA PRODUCCION DE METANOL EN UN REACTOR DE FASE LIQUIDA, A PARTIR DE GAS DE SINTESIS COMPRENDIDO DE HIDROGENO, DIOXIDO DE CARBONO Y MONOXIDO DE CARBONO. EL REACTOR DE FASE LIQUIDA CONTIENEN UN CATALIZDOR SOLIDO SUSPENDIDO EN METANOL. EN ESTA INNOVACION, EL METANOL ACTUA TANTO COMO UN PRODUCTO COMO UN MEDIO DE SUSPENSION PRA EL CATALIZADOR. LA NUEVA INNOVACION EXPLOTA LAS CONDICIONES DE CONDENSACION PARA LA PRODUCCION DE METANOL. OPERANDO A LAS CONDICIONES DE CONDENSACION, LA PRESION PARCIAL DE METANOL EN EL EQUILIBRIO ES MAYOR QUE LA PRESION DE EBULLICION DEL METANOL A LA TEMPERATURA DETERMINADA. DE AQUI QUE EL METANOL PRODUCIDO, DE LA COMPOSICION EN EL EQUILIBRIO, SE CONDENSA CREANDO EL POTENCIAL DE MAS GAS CONVERTIDOR. DADO QUE EL EQUILIBRIO NO ES UN FACTOR LIMITATIVO, SE PUEDEN OBTENER ALTAS CONVERSIONES.
CL200400742A 2003-04-07 2004-04-06 Proceso para preparar ch3oh con un gas de sintesis que contiene co2, el gas reacciona en condiciones de condensacion de ch2oh, el reactor contiene particulas de catalizador suspendidas en ch2oh y agua, y la corriente reciclada comprende al menos uno CL2004000742A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DKPA200300529 2003-04-07

Publications (1)

Publication Number Publication Date
CL2004000742A1 true CL2004000742A1 (es) 2005-03-18

Family

ID=33040861

Family Applications (1)

Application Number Title Priority Date Filing Date
CL200400742A CL2004000742A1 (es) 2003-04-07 2004-04-06 Proceso para preparar ch3oh con un gas de sintesis que contiene co2, el gas reacciona en condiciones de condensacion de ch2oh, el reactor contiene particulas de catalizador suspendidas en ch2oh y agua, y la corriente reciclada comprende al menos uno

Country Status (10)

Country Link
US (1) US6881759B2 (es)
JP (1) JP2004307493A (es)
CN (1) CN100355712C (es)
AR (1) AR043982A1 (es)
AU (1) AU2004201447B2 (es)
CA (1) CA2463346C (es)
CL (1) CL2004000742A1 (es)
NO (1) NO334110B1 (es)
RU (1) RU2360898C2 (es)
ZA (1) ZA200402695B (es)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7608743B2 (en) * 2005-04-15 2009-10-27 University Of Southern California Efficient and selective chemical recycling of carbon dioxide to methanol, dimethyl ether and derived products
EP1871731B1 (en) * 2005-04-15 2012-12-26 University Of Southern California Efficient and selective conversion of carbon dioxide to methanol, dimethyl ether and derived products
US7459486B2 (en) * 2005-07-27 2008-12-02 Exxonmobil Chemical Patents Inc. Making a methanol product in a slurry bubble reactor
DK2021309T3 (da) 2006-05-30 2014-07-21 Starchem Technologies Inc Fremgangsmåde til fremstilling af methanol
US20080260631A1 (en) * 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
US7972415B2 (en) * 2008-12-11 2011-07-05 Spx Corporation Membrane-based compressed air breathing system
PL2571612T3 (pl) 2010-05-20 2015-05-29 Haldor Topsoe As Sposób oraz urządzenie do oddzielania cieczy od strumienia gazu wsadowego w reaktorze katalitycznym
CA2985284C (en) * 2015-05-11 2024-04-30 Haldor Topsoe A/S Use of syngas comprising carbon monoxide and water in the synthesis of methanol
DE102015214943A1 (de) * 2015-08-05 2017-02-09 Siemens Aktiengesellschaft Verfahren und Anlage für eine chemische Synthese
KR102556477B1 (ko) * 2015-11-16 2023-07-18 한국에너지기술연구원 슬러리 반응기를 이용하여 이산화탄소로부터 알코올을 제조하는 방법
FR3045666B1 (fr) * 2015-12-18 2018-02-16 Suez Environnement Procede de synthese de molecules organiques
US10150721B2 (en) 2016-07-15 2018-12-11 Gas Technology Institute Catalytic membrane reactor for dimethyl ether synthesis from carbon dioxide and hydrogen
DE102017206763A1 (de) * 2017-04-21 2018-10-25 Siemens Aktiengesellschaft Verfahren und Vorrichtung zum Umsetzen von Kohlenstoffdioxid zu Methanol
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
CN112292200B (zh) * 2018-06-12 2024-04-12 托普索公司 生产甲醇的方法和设置
CN110903870B (zh) * 2018-09-18 2021-08-20 中国石油化工股份有限公司 浆态床中煤基合成气单次通过制甲烷的工艺
JP7174407B2 (ja) * 2018-12-28 2022-11-17 国立研究開発法人産業技術総合研究所 メトキシプロパノールの製造方法
CA3072183A1 (en) 2019-02-08 2020-08-08 David O. Trahan Methanol production reactor apparatus and method of operation using a homogenous catalyst
EP3714971B1 (en) 2019-03-28 2022-02-02 Sener, Ingeniería y Sistemas, S.A. System for methanol production from a synthesis gas rich in hydrogen and co2/co

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US1302011A (en) * 1918-12-06 1919-04-29 Jens Anton Christiansen Method of producing methyl alcohol from alkyl formates.
JPS57126434A (en) 1981-01-27 1982-08-06 Mitsui Toatsu Chem Inc Synthesis of methanol
WO1984000360A1 (en) * 1982-07-06 1984-02-02 Sintef Method in the production of methyl formate and methanol in a liquid phase
US4628066A (en) * 1986-02-12 1986-12-09 Air Products And Chemicals, Inc. Process for the production of methanol
US4935395A (en) * 1986-12-19 1990-06-19 Associated Universities, Inc. Homogeneous catalyst formulations for methanol production
US4766154A (en) * 1987-02-06 1988-08-23 Air Products And Chemicals, Inc. Liquid phase methanol reactor staging process for the production of methanol
US4910277A (en) * 1988-02-09 1990-03-20 Bambury Ronald E Hydrophilic oxygen permeable polymers
DK163578C (da) * 1990-03-19 1992-08-03 Haldor Topsoe As Fremgangsmaade til fremstilling af metanol
US5179129A (en) * 1991-03-01 1993-01-12 Air Products And Chemicals, Inc. Staged liquid phase methanol process
US5221652A (en) * 1991-03-26 1993-06-22 The University Of Pittsburgh Methanol synthesis using a catalyst combination of alkali or alkaline earth salts and reduced copper chromite for methanol synthesis
EP0555060B1 (en) * 1992-02-04 1996-07-17 Air Products And Chemicals, Inc. Liquid phase methanol process with co-rich recycle
DE4239904C2 (de) * 1992-11-27 2003-06-05 Mg Technologies Ag Verfahren zur Herstellung von Methanol
GB2281224B (en) * 1993-08-24 1998-02-11 Norske Stats Oljeselskap Solid/liquid slurry treatment apparatus and catalytic multi-phase reactor
JPH09249593A (ja) * 1996-03-14 1997-09-22 Sekiyu Sangyo Kasseika Center メタノールの製造方法
JP3553740B2 (ja) * 1996-08-21 2004-08-11 財団法人石油産業活性化センター メタノールの製造方法
JP3506602B2 (ja) * 1997-02-27 2004-03-15 財団法人石油産業活性化センター メタノールの製造方法
JP2002249452A (ja) * 2001-02-22 2002-09-06 Mitsubishi Materials Corp 含酸素化合物の合成装置およびその方法

Also Published As

Publication number Publication date
CN100355712C (zh) 2007-12-19
RU2004110209A (ru) 2005-10-20
US20040198847A1 (en) 2004-10-07
CA2463346A1 (en) 2004-10-07
ZA200402695B (en) 2004-10-14
US6881759B2 (en) 2005-04-19
NO334110B1 (no) 2013-12-09
AU2004201447B2 (en) 2010-03-04
RU2360898C2 (ru) 2009-07-10
AR043982A1 (es) 2005-08-17
JP2004307493A (ja) 2004-11-04
CN1569785A (zh) 2005-01-26
CA2463346C (en) 2012-06-05
AU2004201447A1 (en) 2004-10-21
NO20041415L (no) 2004-10-08

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