ES2050751T3 - Alta produccion volumetrica de metanol en un reactor en fase liquida. - Google Patents

Alta produccion volumetrica de metanol en un reactor en fase liquida.

Info

Publication number
ES2050751T3
ES2050751T3 ES89118402T ES89118402T ES2050751T3 ES 2050751 T3 ES2050751 T3 ES 2050751T3 ES 89118402 T ES89118402 T ES 89118402T ES 89118402 T ES89118402 T ES 89118402T ES 2050751 T3 ES2050751 T3 ES 2050751T3
Authority
ES
Spain
Prior art keywords
methanol
liquid phase
phase reactor
high volumetric
feeding
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
ES89118402T
Other languages
English (en)
Inventor
John Joseph Lewnard
Dennis Mackenzie Brown
Pradip Rao
Robert Fred Rick Weimer
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 ES2050751T3 publication Critical patent/ES2050751T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation 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
    • C07C29/151Preparation 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
    • C07C29/153Preparation 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 the catalyst used
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements 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)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

EL INVENTO SE REFIERE A UN PROCESO PARA MEJORAR LA PRODUCTIVIDAD VOLUMETRICA EN UN REACTOR EN LA PRODUCCION DE METANOL EN EL CUAL UNA CORRIENTE DE GAS DE ALIMENTACION DE SINTESIS CONTENIENDO HIDROGENO Y OXIDOS DE CARBONO SE PONE EN CONTACTO CON UN FANGO CATALIZADOR CONTENIENDO MAS DEL 25% DE SU PESO DE UN CATALIZADOR EN POLVO CONTENIENDO COBRE Y QUE TENGA UNA POROSIDAD DE ENTRE EL 30 AL 70%. LA PRODUCTIVIDAD VOLUMETRICA SE MAXIMIZA EN EL PROCESO CONTROLANDO UN PARAMETRO SIMPLE, LA ALIMENTACION DEL GAS, DONDE LA ALIMENTACION SE MANTIENE DENTRO DEL RANGO DE ENTRE EL 14 AL 26%.
ES89118402T 1988-10-11 1989-10-04 Alta produccion volumetrica de metanol en un reactor en fase liquida. Expired - Lifetime ES2050751T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/255,935 US4910227A (en) 1988-10-11 1988-10-11 High volumetric production of methanol in a liquid phase reactor

Publications (1)

Publication Number Publication Date
ES2050751T3 true ES2050751T3 (es) 1994-06-01

Family

ID=22970454

Family Applications (1)

Application Number Title Priority Date Filing Date
ES89118402T Expired - Lifetime ES2050751T3 (es) 1988-10-11 1989-10-04 Alta produccion volumetrica de metanol en un reactor en fase liquida.

Country Status (7)

Country Link
US (1) US4910227A (es)
EP (1) EP0363802B1 (es)
JP (1) JPH064550B2 (es)
AU (1) AU614878B2 (es)
CA (1) CA1317602C (es)
DE (1) DE68912870T2 (es)
ES (1) ES2050751T3 (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1245393B (it) * 1991-03-22 1994-09-20 Eniricerche Spa Bistema catalitico e procedimento per la produzione di metanolo da gas di sintesi in fase liquida
US6296757B1 (en) 1995-10-17 2001-10-02 Exxon Research And Engineering Company Synthetic diesel fuel and process for its production
US5766274A (en) 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
US6191066B1 (en) 1998-05-27 2001-02-20 Energy International Corporation Fischer-Tropsch activity for non-promoted cobalt-on-alumina catalysts
US6262132B1 (en) * 1999-05-21 2001-07-17 Energy International Corporation Reducing fischer-tropsch catalyst attrition losses in high agitation reaction systems
US6211254B1 (en) 1999-06-07 2001-04-03 John P. Whitney Process for recycling heterogeneous waste
WO2007108014A1 (en) * 2006-03-20 2007-09-27 Cri Ehf Process for producing liquid fuel from carbon dioxide and water
US20080260631A1 (en) * 2007-04-18 2008-10-23 H2Gen Innovations, Inc. Hydrogen production process
US9249064B2 (en) 2009-11-20 2016-02-02 Cri, Ehf Storage of intermittent renewable energy as fuel using carbon containing feedstock
US9423528B2 (en) 2012-06-25 2016-08-23 Johnson & Johnson Vision Care, Inc. Method of making silicone containing contact lens with reduced amount of diluents
AU2022207712A1 (en) 2021-01-15 2023-07-06 Cri Hf Methanol synthesis reactor

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4031123A (en) * 1975-11-21 1977-06-21 Chem Systems Inc. Methanol production in a paraffinic medium
ATE3536T1 (de) * 1980-02-12 1983-06-15 Chem Systems, Inc. Verfahren zur herstellung von methanol.
US4478954A (en) * 1983-05-23 1984-10-23 Standard Oil Company (Indiana) Synthesis gas reaction
FR2566390B1 (fr) * 1984-06-21 1986-10-03 Inst Francais Du Petrole Procede de synthese du methanol en presence d'un catalyseur soluble du cuivre et du zinc a partir d'oxyde de carbone et d'hydrogene
GB8521650D0 (en) * 1985-08-30 1985-10-02 Ici Plc Catalyst
US4628066A (en) * 1986-02-12 1986-12-09 Air Products And Chemicals, Inc. Process for the production of methanol

Also Published As

Publication number Publication date
EP0363802A3 (en) 1991-08-07
JPH02134333A (ja) 1990-05-23
EP0363802A2 (en) 1990-04-18
CA1317602C (en) 1993-05-11
DE68912870T2 (de) 1994-05-19
JPH064550B2 (ja) 1994-01-19
AU4252789A (en) 1990-04-26
US4910227A (en) 1990-03-20
DE68912870D1 (de) 1994-03-17
AU614878B2 (en) 1991-09-12
EP0363802B1 (en) 1994-02-02

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