JP4017725B2 - 酢酸の製造用イリジウム触媒カルボニル化方法 - Google Patents

酢酸の製造用イリジウム触媒カルボニル化方法 Download PDF

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Publication number
JP4017725B2
JP4017725B2 JP35098897A JP35098897A JP4017725B2 JP 4017725 B2 JP4017725 B2 JP 4017725B2 JP 35098897 A JP35098897 A JP 35098897A JP 35098897 A JP35098897 A JP 35098897A JP 4017725 B2 JP4017725 B2 JP 4017725B2
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concentration
iridium
carbonylation
weight
liquid reaction
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Japanese (ja)
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JPH10310549A5 (enExample
JPH10310549A (ja
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グレン サンリー ジョン
ジョン ワット ロバート
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BP Chemicals Ltd
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/12—Preparation 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

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  • 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)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
JP35098897A 1996-12-19 1997-12-19 酢酸の製造用イリジウム触媒カルボニル化方法 Expired - Fee Related JP4017725B2 (ja)

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GBGB9626428.8A GB9626428D0 (en) 1996-12-19 1996-12-19 Process
GB9626428.8 1996-12-19

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JPH10310549A JPH10310549A (ja) 1998-11-24
JPH10310549A5 JPH10310549A5 (enExample) 2005-07-21
JP4017725B2 true JP4017725B2 (ja) 2007-12-05

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US (1) US5883295A (enExample)
EP (1) EP0849251B1 (enExample)
JP (1) JP4017725B2 (enExample)
KR (1) KR100503706B1 (enExample)
CN (1) CN1121370C (enExample)
AR (1) AR010831A1 (enExample)
BR (1) BR9706698A (enExample)
CA (1) CA2225142C (enExample)
DE (1) DE69716860T2 (enExample)
GB (1) GB9626428D0 (enExample)
ID (1) ID19222A (enExample)
MX (1) MX9710428A (enExample)
MY (1) MY118787A (enExample)
NO (1) NO975918L (enExample)
NZ (1) NZ329434A (enExample)
SA (1) SA98190162B1 (enExample)
SG (1) SG73485A1 (enExample)
TW (1) TW412524B (enExample)
UA (1) UA52606C2 (enExample)
ZA (1) ZA9711262B (enExample)

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KR20080108605A (ko) * 2006-04-05 2008-12-15 우드랜드 바이오퓨엘스 인크. 합성 가스에 의해 바이오매스를 에탄올로 전환시키는 시스템 및 방법
US7902398B2 (en) 2007-04-25 2011-03-08 Celanese International Corporation Method and apparatus for carbonylation with reduced catalyst loss
US7989659B2 (en) 2007-05-17 2011-08-02 Celanese International Corporation Method and apparatus for making acetic acid with improved light ends column productivity
US7619113B2 (en) * 2007-09-27 2009-11-17 Celanese International Corporation Method and apparatus for making acetic acid with improved purification
US7902397B2 (en) * 2007-10-11 2011-03-08 Celanese International Corporation Method and apparatus for making acetic acid with improved productivity
US7820855B2 (en) * 2008-04-29 2010-10-26 Celanese International Corporation Method and apparatus for carbonylating methanol with acetic acid enriched flash stream
MX2010011850A (es) 2008-04-29 2010-11-30 Celanese Int Corp Sistema de carbonilacion de metanol que tiene un absorbedor con multiples opciones de disolvente.
US7884237B2 (en) * 2008-11-07 2011-02-08 Celanese International Corp. Methanol carbonylation with improved aldehyde removal
US8168822B2 (en) 2009-07-07 2012-05-01 Celanese International Corporation Acetic acid production by way of carbonylation with enhanced reaction and flashing
US8455685B2 (en) * 2009-07-07 2013-06-04 Celanese International Corporation Acetic anhydride production by way of carbonylation with enhanced reaction and flashing
US8575403B2 (en) 2010-05-07 2013-11-05 Celanese International Corporation Hydrolysis of ethyl acetate in ethanol separation process
US8569551B2 (en) 2010-05-07 2013-10-29 Celanese International Corporation Alcohol production process integrating acetic acid feed stream comprising water from carbonylation process
WO2012148509A1 (en) 2011-04-26 2012-11-01 Celanese International Corporation Process for producing ethanol using a stacked bed reactor
US8710279B2 (en) 2010-07-09 2014-04-29 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US8859827B2 (en) 2011-11-18 2014-10-14 Celanese International Corporation Esterifying acetic acid to produce ester feed for hydrogenolysis
US9272970B2 (en) 2010-07-09 2016-03-01 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US8664454B2 (en) 2010-07-09 2014-03-04 Celanese International Corporation Process for production of ethanol using a mixed feed using copper containing catalyst
US8378141B2 (en) 2010-08-16 2013-02-19 Celanese International Corporation Process and system for supplying vapor from drying column to light ends column
US8530696B2 (en) 2010-09-24 2013-09-10 Celanese International Corporation Pump around reactor for production of acetic acid
US8877963B2 (en) 2010-09-28 2014-11-04 Celanese International Corporation Production of acetic acid with high conversion rate
US8394988B2 (en) 2010-09-28 2013-03-12 Celanese International Corporation Production of acetic acid with high conversion rate
US8461379B2 (en) 2010-10-12 2013-06-11 Celanese International Corporation Production of acetic acid comprising feeding at least one reactant to a recycle stream
CN102442897B (zh) * 2010-10-13 2014-05-28 中国石油化工股份有限公司 一种羰基化反应制备乙酸的方法
CN103153932A (zh) 2010-10-13 2013-06-12 国际人造丝公司 回收卤素促进剂和除去高锰酸盐还原化合物的方法
US8637698B2 (en) 2010-11-19 2014-01-28 Celanese International Corporation Production of acetic acid with an increased production rate
US8563773B2 (en) 2010-12-16 2013-10-22 Celanese International Corporation Eductor-based reactor and pump around loops for production of acetic acid
TW201302684A (zh) 2011-04-26 2013-01-16 Celanese Int Corp 由醋酸進料及再循環醋酸乙酯進料生產乙醇之製程
US8686199B2 (en) 2011-04-26 2014-04-01 Celanese International Corporation Process for reducing the concentration of acetic acid in a crude alcohol product
US8884081B2 (en) 2011-04-26 2014-11-11 Celanese International Corporation Integrated process for producing acetic acid and alcohol
US8754268B2 (en) 2011-04-26 2014-06-17 Celanese International Corporation Process for removing water from alcohol mixtures
US9073816B2 (en) 2011-04-26 2015-07-07 Celanese International Corporation Reducing ethyl acetate concentration in recycle streams for ethanol production processes
US8592635B2 (en) 2011-04-26 2013-11-26 Celanese International Corporation Integrated ethanol production by extracting halides from acetic acid
US8697908B2 (en) 2011-05-05 2014-04-15 Celanese International Corporation Removal of amine compounds from carbonylation process stream containing corrosion metal contaminants
WO2012151377A1 (en) 2011-05-05 2012-11-08 Celanese International Corporation Removal of aromatics from carbonylation process
US8895786B2 (en) 2011-08-03 2014-11-25 Celanese International Corporation Processes for increasing alcohol production
US9663437B2 (en) 2011-09-13 2017-05-30 Celanese International Corporation Production of acetic acid with high conversion rate
US8686201B2 (en) 2011-11-09 2014-04-01 Celanese International Corporation Integrated acid and alcohol production process having flashing to recover acid production catalyst
WO2013070210A1 (en) 2011-11-09 2013-05-16 Celanese International Corporation Integrated carbonylation and hydrogenation process to obtain ethanol having flashing to recover acid production catalyst
US8614359B2 (en) 2011-11-09 2013-12-24 Celanese International Corporation Integrated acid and alcohol production process
WO2013070209A1 (en) 2011-11-09 2013-05-16 Celanese International Corporation Integrated carbonylation and hydrogenation process to obtain ethanol
US8748673B2 (en) 2011-11-18 2014-06-10 Celanese International Corporation Process of recovery of ethanol from hydrogenolysis process
WO2013078207A1 (en) 2011-11-22 2013-05-30 Celanese International Corporation Esterifying an ethanol and acetic acid mixture to produce an ester feed for hydrogenolysis
WO2013078212A1 (en) 2011-11-22 2013-05-30 Celanese International Corporation Hydrogenating acetic acid to produce ethyl acetate and reducing ethyl acetate to ethanol
US9029614B2 (en) 2011-12-14 2015-05-12 Celanese International Corporation Phasing reactor product from hydrogenating acetic acid into ethyl acetate feed to produce ethanol
US20130172633A1 (en) 2011-12-29 2013-07-04 Celanese International Corporation Process For Producing Ethanol From Impure Methanol
BR112013007324B1 (pt) 2012-02-08 2020-10-20 Celanese International Corporation produção de ácido acético com alta taxa de conversão
US8859810B2 (en) 2012-08-21 2014-10-14 Celanese International Corporation Process for recovering permanganate reducing compounds from an acetic acid production process
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US9505691B2 (en) 2014-10-02 2016-11-29 Celanese International Corporation Process for producing acetic acid
US9260369B1 (en) 2014-11-14 2016-02-16 Celanese International Corporation Processes for producing acetic acid product having low butyl acetate content
US9302975B1 (en) 2015-07-01 2016-04-05 Celanese International Corporation Process for flashing a reaction medium
US9487464B2 (en) 2015-01-30 2016-11-08 Celanese International Corporation Processes for producing acetic acid
US9561994B2 (en) 2015-01-30 2017-02-07 Celanese International Corporation Processes for producing acetic acid
US9505696B2 (en) 2015-02-04 2016-11-29 Celanese International Corporation Process to control HI concentration in residuum stream
US9382183B1 (en) 2015-07-01 2016-07-05 Celanese International Corporation Process for flashing a reaction medium
US9302974B1 (en) 2015-07-01 2016-04-05 Celanese International Corporation Process for producing acetic acid
CN108137468B (zh) 2015-10-02 2021-04-13 国际人造丝公司 使用水的再循环生产乙酸的方法
US9908835B2 (en) 2015-11-13 2018-03-06 Celanese International Corporation Processes for purifying acetic and hydrating anhydride
US9957216B2 (en) 2015-11-13 2018-05-01 Celanese International Corporation Processes for producing acetic acid
MX2022015387A (es) 2020-06-03 2023-01-16 Celanese Int Corp Produccion y purificacion de acido acetico.

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SE364254B (enExample) * 1967-04-05 1974-02-18 Monsanto Co
GB9306409D0 (en) * 1993-03-26 1993-05-19 Bp Chem Int Ltd Process
FR2725443B1 (fr) * 1994-10-05 1996-12-20 Rhone Poulenc Chimie Preparation d'acides carboxyliques ou des esters correspondants par carbonylation en presence d'iridium

Also Published As

Publication number Publication date
AR010831A1 (es) 2000-07-12
GB9626428D0 (en) 1997-02-05
SG73485A1 (en) 2000-06-20
CN1121370C (zh) 2003-09-17
DE69716860D1 (de) 2002-12-12
JPH10310549A (ja) 1998-11-24
TW412524B (en) 2000-11-21
KR100503706B1 (ko) 2005-09-26
CN1187483A (zh) 1998-07-15
BR9706698A (pt) 1999-05-18
KR19980064381A (ko) 1998-10-07
NO975918D0 (no) 1997-12-16
CA2225142C (en) 2006-12-05
NZ329434A (en) 2000-05-26
ID19222A (id) 1998-06-28
ZA9711262B (en) 1999-06-15
MY118787A (en) 2005-01-31
EP0849251A1 (en) 1998-06-24
MX9710428A (es) 1998-09-30
NO975918L (no) 1998-06-22
SA98190162B1 (ar) 2006-09-09
UA52606C2 (uk) 2003-01-15
EP0849251B1 (en) 2002-11-06
US5883295A (en) 1999-03-16
DE69716860T2 (de) 2003-07-31
CA2225142A1 (en) 1998-06-19

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