ES2163712T3 - Procedimiento de produccion de acido isoftalico de elevada pureza. - Google Patents

Procedimiento de produccion de acido isoftalico de elevada pureza.

Info

Publication number
ES2163712T3
ES2163712T3 ES97305124T ES97305124T ES2163712T3 ES 2163712 T3 ES2163712 T3 ES 2163712T3 ES 97305124 T ES97305124 T ES 97305124T ES 97305124 T ES97305124 T ES 97305124T ES 2163712 T3 ES2163712 T3 ES 2163712T3
Authority
ES
Spain
Prior art keywords
acid
isoftalic
mother
oxidation
liquor
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.)
Expired - Lifetime
Application number
ES97305124T
Other languages
English (en)
Inventor
Fumio Ohkoshi
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co 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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Application granted granted Critical
Publication of ES2163712T3 publication Critical patent/ES2163712T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • 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
    • 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
    • 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
    • C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PROCEDIMIENTO DE PRODUCCION DE ACIDO ISOFTALICO, QUE COMPRENDE: (A) OXIDACION EN FASE LIQUIDA DE UN COMPUESTO DE M NILENO EN UN DISOLVENTE DE ACIDO ACETICO, PARA FORMAR UNA DISOLUCION DE OXIDACION EN FASE LIQUIDA; (B) CRISTALIZACION DE ACIDO ISOFTALICO BRUTO A PARTIR DE LA SOLUCION DE OXIDACION EN FASE LIQUIDA, PARA OBTENER DE ESTA FORMA EL ACIDO ISOFTALICO BRUTO Y UN LICOR MADRE DE OXIDACION; (C) EVAPORAR AL MENOS UNA PARTE DEL LICOR MADRE DE OXIDACION COMO VAPOR DE ACIDO ACETICO O UN CONDENSADO DEL MISMO; (D) DISOLVER EL ACIDO ISOFTALICO BRUTO EN AGUA, SOMETIENDOLO A CONTINUACION A HIDROGENACION CATALITICA, TRATANDO CATALITICAMENTE U OXIDANDO EL ACIDO ISOFTALICO ACUOSO RESULTANTE PARA OBTENER ASI UNA SOLUCION PURIFICADA; (E) REFRIGERAR LA SOLUCION PURIFICADA PARA CRISTALIZAR EL ACIDO ISOFTALICO Y SEPARAR LOS CRISTALES DE ACIDO ISOFTALICO ASI OBTENIDOS A PARTIR DEL LICOR MADRE; (F) ALIMENTAR EL VAPOR DE ACIDO ACETICO O EL CONDENSADO OBTENIDO POR EVAPORACION DEL LICOR MADRE DE OXIDACION DELA FASE (C) A UNA ETAPA INTERMEDIA DE UNA COLUMNA DE DESTILACION Y ALIMENTAR EL LICOR MADRE SEPARADO A PARTIR DE LA SOLUCION PURIFICADA EN LA FASE (E) A LA ZONA SUPERIOR DE DICHA COLUMNA DE DESTILACION; Y (G) DESCARGAR, A PARTIR DE LA ZONA INFERIOR DE DICHA COLUMNA DE DESTILACION, UNA SOLUCION DE ACIDO ACETICO QUE CONTIENE ACIDOS CARBOXILICOS AROMATICOS.
ES97305124T 1996-07-12 1997-07-11 Procedimiento de produccion de acido isoftalico de elevada pureza. Expired - Lifetime ES2163712T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP18332896A JP3757995B2 (ja) 1996-07-12 1996-07-12 高純度イソフタル酸の製造方法
US08/890,006 US5770765A (en) 1996-07-12 1997-07-08 Process for the production of high-purity isophthalic acid

Publications (1)

Publication Number Publication Date
ES2163712T3 true ES2163712T3 (es) 2002-02-01

Family

ID=26501818

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97305124T Expired - Lifetime ES2163712T3 (es) 1996-07-12 1997-07-11 Procedimiento de produccion de acido isoftalico de elevada pureza.

Country Status (5)

Country Link
US (1) US5770765A (es)
EP (1) EP0818434B1 (es)
JP (1) JP3757995B2 (es)
ES (1) ES2163712T3 (es)
SG (1) SG50861A1 (es)

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US6140534A (en) * 1995-06-07 2000-10-31 Hfm International, Inc. Method for purifying isophthalic acid prepared from metaxylene
GB2355711B (en) 1999-10-27 2003-12-24 Agilent Technologies Inc Porous silica microsphere scavengers
JP5073890B2 (ja) * 2001-06-06 2012-11-14 株式会社ナード研究所 芳香族または複素環カルボン酸類の製造法
US7351396B2 (en) * 2003-06-05 2008-04-01 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
US7410632B2 (en) * 2003-06-05 2008-08-12 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US7494641B2 (en) 2003-06-05 2009-02-24 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
US7452522B2 (en) * 2003-06-05 2008-11-18 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
US7282151B2 (en) * 2003-06-05 2007-10-16 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7381386B2 (en) * 2003-06-05 2008-06-03 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US20050288527A1 (en) * 2004-06-28 2005-12-29 Cook William L Method for preparing free-flowing crystalline material
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7897810B2 (en) 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US20070238899A9 (en) * 2004-09-02 2007-10-11 Robert Lin Optimized production of aromatic dicarboxylic acids
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7888530B2 (en) * 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) * 2004-11-29 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
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 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
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7273559B2 (en) 2004-10-28 2007-09-25 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7291270B2 (en) * 2004-10-28 2007-11-06 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
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
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7462736B2 (en) * 2006-03-01 2008-12-09 Eastman Chemical Company Methods and apparatus for isolating carboxylic acid
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
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
US7863483B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Carboxylic acid production process
US7863481B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US20070208199A1 (en) * 2006-03-01 2007-09-06 Kenny Randolph Parker Methods and apparatus for isolating carboxylic acid
US7847121B2 (en) * 2006-03-01 2010-12-07 Eastman Chemical Company Carboxylic acid production process
US20070203359A1 (en) 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US7714094B2 (en) * 2007-11-15 2010-05-11 Eastman Chemical Company Simplified isophthalic acid process for modifying PET
ITRE20110028A1 (it) * 2011-04-20 2012-10-21 Ufi Innovation Ct Srl Gruppo filtrante
ES2979241T3 (es) * 2017-06-28 2024-09-25 Vitaworks Ip Llc Procedimiento para la separación de ácidos dibásicos y aminoácidos de cadena larga
US10329240B2 (en) 2017-06-28 2019-06-25 Vitaworks Ip, Llc Process for the separation of long chain amino acids and dibasic acids
US10239822B2 (en) 2017-06-28 2019-03-26 Vitaworks Ip, Llc Process for the separation of long chain amino acids and dibasic acids
US9969676B1 (en) * 2017-06-28 2018-05-15 Vitaworks Ip, Llc Process for the separation of long chain amino acids and dibasic acids
WO2024030746A1 (en) * 2022-08-03 2024-02-08 Eastman Chemical Company Recycled content metaxylene and related chemical compounds from waste plastic

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4675438A (en) * 1978-11-17 1987-06-23 Amoco Corporation Direct continuous flow integration of production and purification of high purity iso- or terephthalic acid
US4933492A (en) * 1988-10-13 1990-06-12 Amoco Corporation Purification of crude isophthalic acid
JP2893860B2 (ja) * 1990-05-17 1999-05-24 三菱瓦斯化学株式会社 高純度イソフタル酸の製造法
US5132450A (en) * 1990-06-25 1992-07-21 Mitsubishi Gas Chemical Company, Inc. Process for producing high purity isophthalic acid
US5110984A (en) * 1990-11-06 1992-05-05 Amoco Corporation Process for increasing the yield of purified isophthalic acid and reducing waste-water treatment a
US5362908A (en) * 1993-03-10 1994-11-08 Amoco Corporation Catalyst and method for purifying crude terephthalic acid, isophthalic acid or naphthalene dicarboxylic acid
US5354898A (en) * 1993-06-17 1994-10-11 Amoco Corporation Method for purifying crude aromatic carboxylic acids
KR970000136B1 (ko) * 1993-09-28 1997-01-04 브이.피. 유리예프 고순도 벤젠디카르복실산 이성질체의 제조방법
US5612007A (en) * 1994-10-14 1997-03-18 Amoco Corporation Apparatus for preparing aromatic carboxylic acids with efficient energy recovery

Also Published As

Publication number Publication date
JP3757995B2 (ja) 2006-03-22
SG50861A1 (en) 1998-07-20
US5770765A (en) 1998-06-23
EP0818434B1 (en) 2001-09-26
EP0818434A3 (en) 1998-10-21
EP0818434A2 (en) 1998-01-14
JPH1025266A (ja) 1998-01-27

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