CO4870701A1 - Proceso y planta para reformar materiales de carga que contienen hidrocarburos - Google Patents

Proceso y planta para reformar materiales de carga que contienen hidrocarburos

Info

Publication number
CO4870701A1
CO4870701A1 CO97073894A CO97073894A CO4870701A1 CO 4870701 A1 CO4870701 A1 CO 4870701A1 CO 97073894 A CO97073894 A CO 97073894A CO 97073894 A CO97073894 A CO 97073894A CO 4870701 A1 CO4870701 A1 CO 4870701A1
Authority
CO
Colombia
Prior art keywords
reforming
zone
mixture
vaporous
synthesis gas
Prior art date
Application number
CO97073894A
Other languages
English (en)
Inventor
Simon Robert Early
Timothy Douglas Gamlin
Mark Andrew Linthwaite
Original Assignee
Kvaerner Process Tech 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 Kvaerner Process Tech Ltd filed Critical Kvaerner Process Tech Ltd
Publication of CO4870701A1 publication Critical patent/CO4870701A1/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
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Una planta para la producción de una mezcla de gas de síntesisque contiene óxidos de carbono e hidrógeno a partir de un material de carga que contiene hidrocarburos, caracterizada por comprender:a) Una zona de reformación, adaptada a ser mantenida bajo condiciones de reformación, y la que tiene una pluralidad de cámaras cargadas con un catalizador efectivo para catalizar al menos una reacción de reformación, para reformar una mezcla vaporosa del material de carga que contiene hidrocarburos y un reactivo de reformación para formar la mezcla de gas de síntesis;b) Medios de alimentación del material de carga y reactivo de reformación para alimentar a las cámaras de la zona de reformación una mezcla vaporosa del material de carga que contiene hidrocarburos y el reactivo de reformación;c) Medios de alimentación de combustible para alimentar la zona de reformación con un combustible adecuado para calentar las cámaras;d) Medios para alimentar la zona de reformación con una corriente vaporosa que comprende oxígeno de combustión en el cual el combustible puede ser quemado;e) Una zona de humidificación mantenida bajo condiciones adecuadas para humidificar la mezcla vaporosa que comprende oxígeno de combustión;f) Una zona intercambiadora de calor adaptada para intercambiar calor entre la mezcla de gas de síntesis reformado y la mezcla vaporosa humidificada que comprende oxígeno de combustión;g) Medios para recuperar de la zona inbtercambiadora de calor una mezcla de gas de síntesis enfriada; yh) Medios para recuperar de la zona de reformación una mezcla vaporosa de productos de combustión que comprende los productos de combustión del combustible en la zona de reformación y cualquier material no quemado alimentado a la zona de reformación.
CO97073894A 1996-12-20 1997-12-18 Proceso y planta para reformar materiales de carga que contienen hidrocarburos CO4870701A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP96309421A EP0849245A1 (en) 1996-12-20 1996-12-20 Process and plant for the production of methanol

Publications (1)

Publication Number Publication Date
CO4870701A1 true CO4870701A1 (es) 1999-12-27

Family

ID=8225204

Family Applications (2)

Application Number Title Priority Date Filing Date
CO97073894A CO4870701A1 (es) 1996-12-20 1997-12-18 Proceso y planta para reformar materiales de carga que contienen hidrocarburos
CO97073899A CO4890871A1 (es) 1996-12-20 1997-12-18 Proceso y planta para la produccion de methanol

Family Applications After (1)

Application Number Title Priority Date Filing Date
CO97073899A CO4890871A1 (es) 1996-12-20 1997-12-18 Proceso y planta para la produccion de methanol

Country Status (8)

Country Link
US (2) US6159395A (es)
EP (3) EP0849245A1 (es)
JP (2) JP3787364B2 (es)
AR (2) AR010372A1 (es)
AU (2) AU7871998A (es)
CO (2) CO4870701A1 (es)
DE (2) DE69708322T2 (es)
WO (2) WO1998028071A1 (es)

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WO2013053371A1 (de) † 2011-10-12 2013-04-18 Solarfuel Gmbh Verfahren zum bereitstellen eines methanreichen produktgases sowie dazu geeignete anordnung
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RU2503651C1 (ru) * 2012-09-20 2014-01-10 Марк Юрьевич Богослов Способ получения метанола из углеводородного газа газовых и газоконденсатных месторождений и комплексная установка для его осуществления
JP5925105B2 (ja) * 2012-10-26 2016-05-25 三菱重工業株式会社 サチュレータ及びこれを備える天然ガス改質システム
KR101790102B1 (ko) 2014-08-04 2017-10-25 한국화학연구원 이산화탄소의 배출을 저감시킬 수 있는 고효율 메탄올 생산 방법
KR101766257B1 (ko) 2016-04-07 2017-08-09 대우조선해양 주식회사 해양생산설비의 이산화탄소 전환 시스템 및 방법
EP3290794A1 (en) 2016-09-05 2018-03-07 Technip France Method for reducing nox emission
WO2020219252A2 (en) * 2019-04-24 2020-10-29 Exxonmobil Research And Engineering Company Reverse flow reactors with selective flue gas management
EP3959171A1 (en) * 2019-04-24 2022-03-02 ExxonMobil Research and Engineering Company Reverse flow reactors with selective flue gas cascade
GB201908449D0 (en) 2019-06-12 2019-07-24 Johnson Matthey Davy Technologies Ltd Process for synthesising methanol
GB201908450D0 (en) 2019-06-12 2019-07-24 Johnson Matthey Davy Technologies Ltd Process for synthesising methanol
US11220429B2 (en) 2019-08-26 2022-01-11 Exxonmobil Research And Engineering Company Process intensification for reverse flow reactors
KR20230127991A (ko) * 2020-11-14 2023-09-01 존플로우 리액터 테크놀로지스, 엘엘씨 친환경 메탄올 생산
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Also Published As

Publication number Publication date
AR010373A1 (es) 2000-06-07
AU7871998A (en) 1998-07-17
EP0946275A1 (en) 1999-10-06
US6191174B1 (en) 2001-02-20
EP0849245A1 (en) 1998-06-24
JP2001506921A (ja) 2001-05-29
JP2001507017A (ja) 2001-05-29
DE69715661T2 (de) 2003-01-23
EP0946275B1 (en) 2001-11-14
EP0946475B1 (en) 2002-09-18
US6159395A (en) 2000-12-12
JP3710487B2 (ja) 2005-10-26
WO1998028248A1 (en) 1998-07-02
DE69715661D1 (de) 2002-10-24
AR010372A1 (es) 2000-06-07
JP3787364B2 (ja) 2006-06-21
EP0946475A1 (en) 1999-10-06
WO1998028071A1 (en) 1998-07-02
DE69708322T2 (de) 2002-07-11
CO4890871A1 (es) 2000-02-28
DE69708322D1 (de) 2001-12-20
AU7872698A (en) 1998-07-17

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