AR084329A1 - Proceso para la produccion de acido acetico - Google Patents

Proceso para la produccion de acido acetico

Info

Publication number
AR084329A1
AR084329A1 ARP110104732A ARP110104732A AR084329A1 AR 084329 A1 AR084329 A1 AR 084329A1 AR P110104732 A ARP110104732 A AR P110104732A AR P110104732 A ARP110104732 A AR P110104732A AR 084329 A1 AR084329 A1 AR 084329A1
Authority
AR
Argentina
Prior art keywords
eductor
acetic acid
suction pump
pump current
reactor based
Prior art date
Application number
ARP110104732A
Other languages
English (en)
Original Assignee
Celanese Int Corp
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 Celanese Int Corp filed Critical Celanese Int Corp
Publication of AR084329A1 publication Critical patent/AR084329A1/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/12Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
    • 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
    • Y02P20/582Recycling of unreacted starting or intermediate materials
    • 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
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)

Abstract

Reivindicación 1: Un procedimiento para producir ácido acético, que comprende las etapas de: hacer reaccionar monóxido de carbono con, por lo menos, un reactivo en un reactor basado en un eductor que contiene un medio de reacción para producir una solución de la reacción que comprende ácido acético, en el que, por lo menos, un reactivo seleccionado del grupo que consiste en metanol, acetato de metilo, formiato de metilo, dimetil éter y mezclas de los mismos, y en donde el medio de reacción comprende agua, ácido acético, acetato de metilo, yoduro de metilo, y un catalizador, en la que el reactor basado en un eductor comprende uno o más mezcladores eductores; extraer la solución de la reacción a una primera velocidad de flujo desde el reactor basado en un eductor; separar una parte de la solución de la reacción para formar una corriente de la bomba de succión; pasar, opcionalmente, una parte de la corriente de la bomba de succión a través de uno o más generadores de vapor para producir una corriente del proceso de salida y vapor; pasar, opcionalmente, una parte de la corriente de la bomba de succión a través de uno o más intercambiadores de calor para producir un flujo de salida, y alimentar una parte de uno o más de los siguientes: la corriente de la bomba de succión, la corriente del proceso de salida, o el flujo de salida de, por lo menos, uno o más mezcladores eductores para proporcionar la mezcla del medio de reacción en el reactor basado en un eductor.
ARP110104732A 2010-12-16 2011-12-16 Proceso para la produccion de acido acetico AR084329A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12/970,315 US8563773B2 (en) 2010-12-16 2010-12-16 Eductor-based reactor and pump around loops for production of acetic acid

Publications (1)

Publication Number Publication Date
AR084329A1 true AR084329A1 (es) 2013-05-08

Family

ID=45464838

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP110104732A AR084329A1 (es) 2010-12-16 2011-12-16 Proceso para la produccion de acido acetico

Country Status (12)

Country Link
US (2) US8563773B2 (es)
EP (1) EP2651869B1 (es)
JP (2) JP2014510700A (es)
CN (1) CN103328429A (es)
AR (1) AR084329A1 (es)
BR (1) BR112013015206A2 (es)
CA (1) CA2821259A1 (es)
MX (1) MX2013006870A (es)
RU (1) RU2013132708A (es)
SG (1) SG191128A1 (es)
TW (1) TWI562984B (es)
WO (1) WO2012082485A2 (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8563773B2 (en) * 2010-12-16 2013-10-22 Celanese International Corporation Eductor-based reactor and pump around loops for production of acetic acid
CN104028178B (zh) * 2013-03-06 2016-03-02 中石化上海工程有限公司 强化水力学反应器混合效果的方法
KR102331722B1 (ko) * 2014-12-31 2021-11-29 삼성에스디아이 주식회사 반응기, 이를 이용한 리튬이차전지의 양극활물질 전구체 제조방법, 그로부터 제조된 전구체, 그를 포함하는 양극 활물질

Family Cites Families (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3522017A (en) * 1964-07-13 1970-07-28 Celanese Corp Reactor for conducting controlledtemperature gas phase reactions with mixing
US3769329A (en) 1970-03-12 1973-10-30 Monsanto Co Production of carboxylic acids and esters
US4140625A (en) * 1977-12-19 1979-02-20 Uop Inc. Mixed-phase distributor for fixed-bed catalytic reaction chambers
US5026908A (en) 1984-05-03 1991-06-25 Hoechst Celanese Corporation Methanol carbonylation process
US5144068A (en) 1984-05-03 1992-09-01 Hoechst Celanese Corporation Methanol carbonylation process
US5001259A (en) 1984-05-03 1991-03-19 Hoechst Celanese Corporation Methanol carbonylation process
CA1299195C (en) 1986-06-16 1992-04-21 G. Paull Torrence Addition of hydrogen to carbon monoxide feed gas in producing acetic acid by carbonylation of methanol
US5672743A (en) 1993-09-10 1997-09-30 Bp Chemicals Limited Process for the production of acetic acid
US5364963A (en) 1993-04-30 1994-11-15 Chiyoda Corporation Supported rhodium catalyst, method of preparing same and process of producing acetic acid by methanol carbonylation using same
JP2662683B2 (ja) * 1993-04-30 1997-10-15 千代田化工建設株式会社 カルボニル化反応用固体触媒及びそれを用いる酢酸の製造方法
US5352415A (en) * 1993-09-29 1994-10-04 Hoechst Celanese Corporation Control system for acetic acid manufacturing process
JP3308392B2 (ja) 1994-06-02 2002-07-29 ダイセル化学工業株式会社 カルボニル化反応方法
US5696284A (en) 1995-06-21 1997-12-09 Bp Chemicals Limited Process for the carbonylation of alkyl alcohols and/or reactive derivatives thereof
PL185073B1 (pl) 1995-10-27 2003-02-28 Celanese Int Corp Sposób polepszania wydajności roztworu katalizatora do karbonylowania oraz sposób karbonylowania metanolu do kwasu octowego
US6339171B1 (en) 1996-10-18 2002-01-15 Celanese International Corporation Removal or reduction of permanganate reducing compounds and alkyl iodides from a carbonylation process stream
GB9625335D0 (en) 1996-12-05 1997-01-22 Bp Chem Int Ltd Process
GB9626429D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
GB9626428D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
GB9626317D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
US6114576A (en) 1997-12-18 2000-09-05 Uop Llc Carbonylation process with integrated heat exchange
ES2216385T3 (es) 1998-08-06 2004-10-16 Haldor Topsoe A/S Proceso de destilacion reactiva de acido acetico basado en la carbonilacion de dme/metanol.
DE19854637A1 (de) * 1998-11-26 2000-05-31 Basf Ag Reaktor zur kontinuierlichen Durchführung von Gas-Flüssig-, Flüssig-Flüssig- oder Gas-Flüssig-Fest-Reaktionen
US6627770B1 (en) 2000-08-24 2003-09-30 Celanese International Corporation Method and apparatus for sequesting entrained and volatile catalyst species in a carbonylation process
US6657078B2 (en) 2001-02-07 2003-12-02 Celanese International Corporation Low energy carbonylation process
JP5069827B2 (ja) * 2001-02-28 2012-11-07 株式会社ダイセル 反応制御方法および制御装置
JP3853664B2 (ja) * 2002-02-04 2006-12-06 松下環境空調エンジニアリング株式会社 薬液調製装置
US7005541B2 (en) 2002-12-23 2006-02-28 Celanese International Corporation Low water methanol carbonylation process for high acetic acid production and for water balance control
JP4388753B2 (ja) * 2003-03-13 2009-12-24 千代田化工建設株式会社 不均一系触媒を用いた酢酸の製造方法
MY141209A (en) 2003-03-13 2010-03-31 Chiyoda Corp Method of manufacturing acetic acid
CA2540712A1 (en) * 2003-10-03 2005-04-14 O.K. Technologies, Llc Waste water treatment system and process
US7223886B2 (en) 2004-03-02 2007-05-29 Celanese International Corporation Removal of permanganate reducing compounds from methanol carbonylation process stream
US7465823B2 (en) 2004-03-17 2008-12-16 Celanese International Corporation Utilization of acetic acid reaction heat in other process plants
ATE506338T1 (de) * 2005-12-21 2011-05-15 Bp Chem Int Ltd Carbonylierungsverfahren
US7989659B2 (en) 2007-05-17 2011-08-02 Celanese International Corporation Method and apparatus for making acetic acid with improved light ends column productivity
US8017802B2 (en) 2007-05-21 2011-09-13 Celanese International Corporation Control of impurities in reaction product of rhodium-catalyzed methanol carbonylation
US8062482B2 (en) 2007-10-30 2011-11-22 Celanese International Corporation Acetaldehyde removal from methyl acetate by distillation at elevated pressure
ES2523719T3 (es) 2008-04-29 2014-12-01 Celanese International Corporation Sistema de carbonilación de metanol que tiene un absorbente con opciones de disolvente múltiples
ES2676645T3 (es) * 2009-05-20 2018-07-23 Xyleco, Inc. Procesamiento de biomasa
CN101885678B (zh) * 2010-07-05 2013-03-13 兖矿国泰化工有限公司 一种甲醇低压羰基化合成醋酸用反应设备
US8530696B2 (en) 2010-09-24 2013-09-10 Celanese International Corporation Pump around reactor for production of acetic acid
US8563773B2 (en) * 2010-12-16 2013-10-22 Celanese International Corporation Eductor-based reactor and pump around loops for production of acetic acid

Also Published As

Publication number Publication date
JP2017014200A (ja) 2017-01-19
MX2013006870A (es) 2013-07-05
JP2014510700A (ja) 2014-05-01
JP6363132B2 (ja) 2018-07-25
US20140018571A1 (en) 2014-01-16
EP2651869B1 (en) 2019-09-11
US20120157710A1 (en) 2012-06-21
EP2651869A2 (en) 2013-10-23
RU2013132708A (ru) 2015-01-27
TWI562984B (en) 2016-12-21
TW201233669A (en) 2012-08-16
SG191128A1 (en) 2013-07-31
CA2821259A1 (en) 2012-06-21
CN103328429A (zh) 2013-09-25
BR112013015206A2 (pt) 2016-09-13
US8563773B2 (en) 2013-10-22
WO2012082485A3 (en) 2012-09-20
WO2012082485A2 (en) 2012-06-21
US9346733B2 (en) 2016-05-24

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