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AR035992A1 - Proceso para producir acido tereftalico puro con recuperacion mejorada de precursores, solvente y metil acetato - Google Patents

Proceso para producir acido tereftalico puro con recuperacion mejorada de precursores, solvente y metil acetato

Info

Publication number
AR035992A1
AR035992A1 ARP000104953A ARP000104953A AR035992A1 AR 035992 A1 AR035992 A1 AR 035992A1 AR P000104953 A ARP000104953 A AR P000104953A AR P000104953 A ARP000104953 A AR P000104953A AR 035992 A1 AR035992 A1 AR 035992A1
Authority
AR
Argentina
Prior art keywords
acid
methyl acetate
terephthalic acid
recover
acetic acid
Prior art date
Application number
ARP000104953A
Other languages
English (en)
Inventor
William David Parten
Original Assignee
Du Pont
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 Du Pont filed Critical Du Pont
Publication of AR035992A1 publication Critical patent/AR035992A1/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; 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)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Proceso continuo para producir ácido tereftálico puro de fórmula (1), mediante (a) primero hacer reaccionar el paraxileno con aire en presencia de ácido acético y un catalizador, a una presión y temperatura elevados para producir ácido tereftálico crudo; (b) recuperar el ácido tereftálico crudo, y una cantidad de ácido acético residual y ácido paratoluico, en forma de una torta húmeda; y (c) purificar el ácido tereftálico crudo al mezclarlo con agua y elevar la temperatura y presión de la mezcla para formar una solución acuosa, poner en contacto la solución acuosa con hidrógeno en presencia de un catalizador, ajustar la presión y temperatura de la solución hidrogenada mientras que se precipitan los cristales puros de ácido tereftálico, y el ácido acético residual y el ácido paratoluico residual permanecen en la solución hidrgenada para formar un licor madre purificado en planta, y recuperar los cristales puros de ácido tereftálico a partir del licor madre purificado en planta que comprende: (i) poner en contacto este licor madre purificado en planta con el paraxileno para formar un sistema de dos fases que comprende: una fase acuosa que contiene un ácido residual, y una fase orgánica que contiene ácido paratoluico y paraxileno; (ii) regresar la fase orgánica a la reacción de oxidación de la etapa (a); (iii) alimentar la fase acuosa a por lo menos un dispositivo de contacto adicional de manera simultánea con una corriente condensada que contiene agua, metil acetato y componentes orgánicos para formar una segunda fase acuosa y una segunda fase orgánica, mediante la cual el metil acetato y el ácido acético residual se particionan; y (iv) recuperar el metil acetato a partir de la segunda fase acuosa y recuperar el ácido acético a partir de la segunda fase orgánica. Este método permite recuperar y/o reciclar los precursores del ácido tereftálico, ácido acético residual y otros subproductos de las reacciones tal como el metil acetato.
ARP000104953A 1999-09-21 2000-09-21 Proceso para producir acido tereftalico puro con recuperacion mejorada de precursores, solvente y metil acetato AR035992A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/400,035 US6143926A (en) 1999-09-21 1999-09-21 Process for producing pure terephthalic acid with improved recovery of precursors, solvent and methyl acetate

Publications (1)

Publication Number Publication Date
AR035992A1 true AR035992A1 (es) 2004-08-04

Family

ID=23581959

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP000104953A AR035992A1 (es) 1999-09-21 2000-09-21 Proceso para producir acido tereftalico puro con recuperacion mejorada de precursores, solvente y metil acetato

Country Status (19)

Country Link
US (1) US6143926A (es)
EP (1) EP1214285B1 (es)
JP (1) JP2003509484A (es)
KR (1) KR100658555B1 (es)
CN (1) CN1374937A (es)
AR (1) AR035992A1 (es)
AT (1) ATE254591T1 (es)
BR (1) BR0014479A (es)
CA (1) CA2380625C (es)
DE (1) DE60006694T2 (es)
DZ (1) DZ3061A1 (es)
EG (1) EG22730A (es)
ES (1) ES2209953T3 (es)
MX (1) MXPA02003036A (es)
MY (1) MY128616A (es)
TR (1) TR200200715T2 (es)
TW (1) TW506965B (es)
WO (1) WO2001021571A1 (es)
ZA (1) ZA200200892B (es)

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100402482C (zh) * 2003-02-21 2008-07-16 三菱化学株式会社 芳香羧酸的制备方法
US7049465B2 (en) * 2003-07-10 2006-05-23 Eastman Chemical Company Process for energy recovery in processes for the preparation of aromatic carboxylic acids
KR100650536B1 (ko) * 2003-12-19 2006-11-27 미쓰이 가가쿠 가부시키가이샤 테레프탈산의 제조 방법
US7213540B2 (en) * 2004-02-05 2007-05-08 Eastman Chemical Company Steam recompression in carboxylic acid processes
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
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 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
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
CN1300088C (zh) * 2005-03-25 2007-02-14 扬子石油化工股份有限公司 一种回收芳香族羧酸生产过程中原料、溶剂和副产物的方法
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
KR100733400B1 (ko) * 2005-08-01 2007-06-29 아신기술 주식회사 아세트산, 메틸아세테이트 및 물을 분리하기 위한공비증류공정
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
US8173835B2 (en) * 2006-03-01 2012-05-08 Grupo Petrotemex, S.A. De C.V. Method and apparatus for drying carboxylic acid
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
KR100860343B1 (ko) * 2007-03-15 2008-09-26 삼성석유화학(주) 친환경적이고 단순화된 방향족 디카르복실산의 제조방법
US9040746B2 (en) * 2008-03-18 2015-05-26 Gtc Technology Us, Llc Systems and processes for the production of isophthalic acid and terephthalic acid
US8382961B2 (en) * 2010-06-07 2013-02-26 Amt International, Inc. System and method for reduction of water consumption in purified terephthalic acid production
US20140121406A1 (en) * 2012-10-31 2014-05-01 Invista North America S.A.R.L. Pure plant mother liquor solvent extraction system and method
JP2015140342A (ja) * 2014-01-30 2015-08-03 株式会社日立製作所 精製テレフタル酸の製造方法
TW201602078A (zh) * 2014-04-08 2016-01-16 英威達技術有限公司 在經純化對苯二甲酸(pta)純化廠中最小化對-甲苯甲酸之回收
CN114181065B (zh) * 2021-12-24 2022-12-20 福州大学 一种节能降耗型的精对苯二甲酸生产方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2833816A (en) * 1954-05-03 1958-05-06 Mid Century Corp Preparation of aromatic polycarboxylic acids
US4172209A (en) * 1978-08-23 1979-10-23 Uop Inc. Process for producing dicarboxylic acids by the oxidation of xylene
US4500732A (en) * 1983-09-15 1985-02-19 Standard Oil Company (Indiana) Process for removal and recycle of p-toluic acid from terephthalic acid crystallizer solvent
JP3729284B2 (ja) * 1995-09-22 2005-12-21 三菱瓦斯化学株式会社 高純度テレフタル酸の製造方法
TW483886B (en) * 1998-08-11 2002-04-21 Du Pont Method for recovering methyl acetate and residual acetic acid in the production of pure terephtalic acid

Also Published As

Publication number Publication date
MY128616A (en) 2007-02-28
CN1374937A (zh) 2002-10-16
TR200200715T2 (tr) 2002-09-23
CA2380625C (en) 2008-07-29
ES2209953T3 (es) 2004-07-01
DE60006694D1 (de) 2003-12-24
DZ3061A1 (fr) 2004-05-26
DE60006694T2 (de) 2004-12-09
JP2003509484A (ja) 2003-03-11
BR0014479A (pt) 2002-06-18
KR20020029137A (ko) 2002-04-17
KR100658555B1 (ko) 2006-12-18
ATE254591T1 (de) 2003-12-15
WO2001021571A1 (en) 2001-03-29
CA2380625A1 (en) 2001-03-29
ZA200200892B (en) 2003-03-26
EP1214285A1 (en) 2002-06-19
TW506965B (en) 2002-10-21
EG22730A (en) 2003-07-30
MXPA02003036A (es) 2002-10-23
EP1214285B1 (en) 2003-11-19
US6143926A (en) 2000-11-07

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