CL2021002893A1 - Proceso para sintetizar metanol - Google Patents

Proceso para sintetizar metanol

Info

Publication number
CL2021002893A1
CL2021002893A1 CL2021002893A CL2021002893A CL2021002893A1 CL 2021002893 A1 CL2021002893 A1 CL 2021002893A1 CL 2021002893 A CL2021002893 A CL 2021002893A CL 2021002893 A CL2021002893 A CL 2021002893A CL 2021002893 A1 CL2021002893 A1 CL 2021002893A1
Authority
CL
Chile
Prior art keywords
gas
methanol
carbon
gas mixture
reformer
Prior art date
Application number
CL2021002893A
Other languages
English (en)
Inventor
Simon Robert Early
Original Assignee
Johnson Matthey Davy Technologies Ltd
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 Johnson Matthey Davy Technologies Ltd filed Critical Johnson Matthey Davy Technologies Ltd
Publication of CL2021002893A1 publication Critical patent/CL2021002893A1/es

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
    • C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/02—Monohydroxylic acyclic alcohols
    • C07C31/04—Methanol
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

Se describe un proceso para sintetizar metanol que comprende las etapas de (i) formar un gas de síntesis que contiene hidrógeno, monóxido de carbono y dióxido de carbono a partir de una materia prima de hidrocarburo en una unidad reformadora que comprende un reformador de intercambio de calor y reformador autotérmico en serie; (ii) enfriar el gas de síntesis en el reformador de intercambio de calor y una o más etapas adicionales de intercambio de calor, y recuperar condensado del proceso a partir del gas de síntesis enfriado para formar un gas auxiliar; (iii) pasar un gas de alimentación que comprende el gas auxiliar a un circuito cerrado de síntesis de metanol que comprende uno o más reactores de síntesis de metanol; (iv) recuperar una mezcla de gases de producto que contiene metanol del circuito cerrado de síntesis de metanol, enfriar la mezcla de gases de producto hasta por debajo del punto de rocío para condensar metanol crudo, y separar el metanol crudo de una mezcla de gases sin reaccionar; y (v) reciclar una porción de la mezcla de gases sin reaccionar al circuito cerrado de síntesis de metanol y recuperar una porción de la mezcla de gases sin reaccionar como una corriente de gas de purga, en donde una corriente rica en hidrógeno y una corriente rica en carbono se separan del gas de purga, una porción de la corriente rica en hidrógeno se alimenta al circuito cerrado de síntesis de metanol y una porción de la corriente rica en carbono se alimenta a la unidad reformadora.
CL2021002893A 2019-06-12 2021-11-03 Proceso para sintetizar metanol CL2021002893A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GBGB1908449.0A GB201908449D0 (en) 2019-06-12 2019-06-12 Process for synthesising methanol

Publications (1)

Publication Number Publication Date
CL2021002893A1 true CL2021002893A1 (es) 2022-06-03

Family

ID=67386113

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2021002893A CL2021002893A1 (es) 2019-06-12 2021-11-03 Proceso para sintetizar metanol

Country Status (12)

Country Link
US (1) US11851393B2 (es)
EP (1) EP3983366B1 (es)
CN (1) CN113784940B (es)
AU (1) AU2020290690B2 (es)
CA (1) CA3137256A1 (es)
CL (1) CL2021002893A1 (es)
DK (1) DK3983366T3 (es)
EA (1) EA202192749A1 (es)
GB (2) GB201908449D0 (es)
MY (1) MY207760A (es)
NZ (1) NZ781400A (es)
WO (1) WO2020249924A1 (es)

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* Cited by examiner, † Cited by third party
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JP7151832B1 (ja) 2021-06-11 2022-10-12 Jfeスチール株式会社 膜反応器における未利用ガスの再利用方法
WO2023194286A1 (en) * 2022-04-08 2023-10-12 Topsoe A/S Methanol loop revamp by co intensification
CA3244658A1 (en) 2022-05-09 2023-11-16 Johnson Matthey Davy Technologies Limited METHANOL SYNTHESIS PROCESS
US12565423B2 (en) 2023-01-26 2026-03-03 Valero Services, Inc. Process for producing hydrogen from natural gas
CN120826385A (zh) 2023-05-26 2025-10-21 庄信万丰戴维科技有限公司 用于合成甲醇的方法

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US4127389A (en) 1977-04-04 1978-11-28 Pullman Incorporated Exchanger reactor
JPS5839572B2 (ja) 1979-04-03 1983-08-31 東洋エンジニアリング株式会社 反応器およびその使用法
EP0026057B1 (en) 1979-09-14 1984-03-14 Imperial Chemical Industries Plc Synthesis reactor and processes
GB8521650D0 (en) 1985-08-30 1985-10-02 Ici Plc Catalyst
GB8803766D0 (en) * 1988-02-18 1988-03-16 Ici Plc Methanol
ATE156778T1 (de) * 1991-07-09 1997-08-15 Ici Plc Synthesegaserzeugung
GB9516125D0 (en) * 1995-08-07 1995-10-04 Ici Plc Heat exchange apparatus and process
DE19605572A1 (de) 1996-02-15 1997-08-21 Metallgesellschaft Ag Verfahren zum Erzeugen von Methanol
EP0849245A1 (en) 1996-12-20 1998-06-24 Kvaerner Process Technology Limited Process and plant for the production of methanol
DK1008577T4 (da) 1998-12-07 2006-06-06 Mitsubishi Heavy Ind Ltd Fremgangsmåde til fremstilling af methanol
NO314496B1 (no) * 2001-06-27 2003-03-31 Statoil Asa I & K Ir Pat Fremgangsmåte for öking av produksjon i et eksisterende prosessanlegg samtet prosessanlegg
WO2005070855A1 (en) * 2004-01-22 2005-08-04 Acetex (Cyprus) Limited Integrated process for acetic acid and methanol
GB0418654D0 (en) 2004-08-20 2004-09-22 Davy Process Techn Ltd Process
GB0507269D0 (en) * 2005-04-11 2005-05-18 Johnson Matthey Plc Steam reforming
GB0510823D0 (en) 2005-05-27 2005-07-06 Johnson Matthey Plc Methanol synthesis
DE102006023248C5 (de) 2006-05-18 2018-01-25 Air Liquide Global E&C Solutions Germany Gmbh Verfahren und Anlage zur Herstellung von Synthesegas
US20090184293A1 (en) * 2008-01-18 2009-07-23 Han Pat A Process for reforming hydrocarbons
US7876211B2 (en) 2008-02-21 2011-01-25 Honeywell International Inc. Apparatus and method for alarm suppression in a monitoring system
EP2228358A1 (en) * 2009-03-13 2010-09-15 Methanol Casale S.A. Recovery of CO2 in a process for synthesis of methanol
US8309617B2 (en) * 2009-12-31 2012-11-13 Phillips 66 Company Recycling methane-rich purge gas to gasifier
CN102844267A (zh) * 2010-01-19 2012-12-26 赫多特普索化工设备公司 重整烃的方法
GB201107072D0 (en) 2011-04-27 2011-06-08 Davy Process Techn Ltd Process
CN107635956B (zh) * 2015-05-11 2020-11-13 托普索公司 一种用于甲醇合成的新方法
GB201600793D0 (en) 2016-01-15 2016-03-02 Johnson Matthey Davy Technologies Ltd Methanol process
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Also Published As

Publication number Publication date
NZ781400A (en) 2026-02-27
CN113784940A (zh) 2021-12-10
AU2020290690A1 (en) 2021-11-11
WO2020249924A1 (en) 2020-12-17
MY207760A (en) 2025-03-17
EA202192749A1 (ru) 2022-03-28
GB2585478B (en) 2021-10-06
DK3983366T3 (da) 2023-07-31
US11851393B2 (en) 2023-12-26
US20220185753A1 (en) 2022-06-16
CN113784940B (zh) 2025-01-28
GB2585478A (en) 2021-01-13
EP3983366B1 (en) 2023-06-28
GB202006892D0 (en) 2020-06-24
GB201908449D0 (en) 2019-07-24
CA3137256A1 (en) 2020-12-17
EP3983366A1 (en) 2022-04-20
AU2020290690B2 (en) 2025-04-10

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