AU2001232878A1 - Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent - Google Patents

Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent

Info

Publication number
AU2001232878A1
AU2001232878A1 AU2001232878A AU3287801A AU2001232878A1 AU 2001232878 A1 AU2001232878 A1 AU 2001232878A1 AU 2001232878 A AU2001232878 A AU 2001232878A AU 3287801 A AU3287801 A AU 3287801A AU 2001232878 A1 AU2001232878 A1 AU 2001232878A1
Authority
AU
Australia
Prior art keywords
aromatic
acid
oxidation
high pressure
reaction medium
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.)
Abandoned
Application number
AU2001232878A
Other languages
English (en)
Inventor
Kenneth J Abrams
Thomas M. Bartos
Alpen K. Pandya
David L Sikkenga
Ian C. Zaenger
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.)
BP Corp North America Inc
Original Assignee
BP Corp North America 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 BP Corp North America Inc filed Critical BP Corp North America Inc
Publication of AU2001232878A1 publication Critical patent/AU2001232878A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
AU2001232878A 2000-01-21 2001-01-19 Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent Abandoned AU2001232878A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US17742900P 2000-01-21 2000-01-21
US60177429 2000-01-21
PCT/US2001/001909 WO2001053246A1 (en) 2000-01-21 2001-01-19 Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent

Publications (1)

Publication Number Publication Date
AU2001232878A1 true AU2001232878A1 (en) 2001-07-31

Family

ID=22648562

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2001232878A Abandoned AU2001232878A1 (en) 2000-01-21 2001-01-19 Production of high purity aromatic carboxylic acid by oxidation in benzoic acid and water solvent

Country Status (13)

Country Link
US (1) US6562997B2 (ru)
EP (1) EP1257520A1 (ru)
JP (1) JP2003520263A (ru)
KR (1) KR20020069261A (ru)
CN (1) CN1227208C (ru)
AU (1) AU2001232878A1 (ru)
BR (1) BR0107739A (ru)
CA (1) CA2396967A1 (ru)
MX (1) MXPA02007123A (ru)
RU (1) RU2259346C2 (ru)
TR (1) TR200201833T2 (ru)
UA (1) UA73971C2 (ru)
WO (1) WO2001053246A1 (ru)

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PT1791800T (pt) * 2004-09-02 2018-02-02 Grupo Petrotemex Sa De Cv Oxidação em fase líquida optimizada
US7897810B2 (en) 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7888530B2 (en) * 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7615663B2 (en) * 2004-09-02 2009-11-10 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
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US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
CN101693655B (zh) * 2004-09-02 2014-01-08 奇派特石化有限公司 优化的液相氧化方法
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
CN101146756B (zh) * 2005-03-21 2011-05-18 Bp北美公司 用于制造纯形式的芳族羧酸的方法和设备
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7569722B2 (en) * 2005-08-11 2009-08-04 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7402694B2 (en) * 2005-08-11 2008-07-22 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
KR100744754B1 (ko) * 2005-12-13 2007-08-01 삼성석유화학(주) 방향족 카르복실산의 제조방법
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US20070208199A1 (en) * 2006-03-01 2007-09-06 Kenny Randolph Parker Methods and apparatus for isolating carboxylic acid
US7863481B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US8173835B2 (en) * 2006-03-01 2012-05-08 Grupo Petrotemex, S.A. De C.V. Method and apparatus for drying carboxylic acid
US7880032B2 (en) * 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7420082B2 (en) * 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7393973B2 (en) * 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US8697906B2 (en) * 2006-03-01 2014-04-15 Grupo Petrotemex, S.A. De C.V. Methods and apparatus for producing a low-moisture carboxylic acid wet cake
US7326807B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system with enhanced heating for oxidative digestion
US7326808B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7501537B2 (en) * 2006-03-01 2009-03-10 Eastman Chemical Company Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange
US7462736B2 (en) * 2006-03-01 2008-12-09 Eastman Chemical Company Methods and apparatus for isolating carboxylic acid
US20070203359A1 (en) * 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7863483B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Carboxylic acid production process
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7847121B2 (en) * 2006-03-01 2010-12-07 Eastman Chemical Company Carboxylic acid production process
US7465824B2 (en) * 2007-02-08 2008-12-16 Bp Corporation North America Inc. Process for the production of high purity aromatic carboxylic acids using a benzoic acid and water solvent for oxidation and purification
US8455680B2 (en) * 2008-01-15 2013-06-04 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8614350B2 (en) 2008-01-15 2013-12-24 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
CN101531588B (zh) * 2008-03-13 2016-02-24 周向进 一种新的精对苯二甲酸的制造方法
WO2009117487A2 (en) 2008-03-18 2009-09-24 Gtc Technology, Lp Improved systems and processes for the production of isophthalic acid and terephthalic acid
CN101575284B (zh) * 2008-05-05 2014-11-26 周向进 一种新的精间苯二甲酸的制造方法
CN101362687B (zh) * 2008-10-08 2012-04-11 湖南大学 空气氧化对二甲苯制备对苯二甲酸的方法和设备
JP5574509B2 (ja) * 2009-03-17 2014-08-20 テイジン・アラミド・ビー．ブイ． 芳香族アルデヒドの芳香族アシルハライドへの変換方法
CN102652122B (zh) * 2009-12-16 2015-09-09 英威达技术有限公司 生产芳香羧酸的系统和方法
US9024059B2 (en) 2011-12-29 2015-05-05 Uop Llc Process for producing terephthalic acid
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CN108017532A (zh) * 2016-10-28 2018-05-11 中国石油化工股份有限公司 一种间二甲苯液相氧化生成间苯二甲酸的方法

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Also Published As

Publication number Publication date
TR200201833T2 (tr) 2002-12-23
RU2259346C2 (ru) 2005-08-27
US20010041811A1 (en) 2001-11-15
WO2001053246A1 (en) 2001-07-26
EP1257520A1 (en) 2002-11-20
CN1395554A (zh) 2003-02-05
CA2396967A1 (en) 2001-07-26
JP2003520263A (ja) 2003-07-02
RU2002121869A (ru) 2004-01-10
UA73971C2 (en) 2005-10-17
BR0107739A (pt) 2002-10-22
MXPA02007123A (es) 2002-12-13
KR20020069261A (ko) 2002-08-29
CN1227208C (zh) 2005-11-16
US6562997B2 (en) 2003-05-13

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