TW280815B - - Google Patents

Info

Publication number
TW280815B
TW280815B TW083109260A TW83109260A TW280815B TW 280815 B TW280815 B TW 280815B TW 083109260 A TW083109260 A TW 083109260A TW 83109260 A TW83109260 A TW 83109260A TW 280815 B TW280815 B TW 280815B
Authority
TW
Taiwan
Application number
TW083109260A
Other languages
Chinese (zh)
Original Assignee
Ici Plc
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
Priority claimed from GB929211441A external-priority patent/GB9211441D0/en
Priority claimed from GB929223966A external-priority patent/GB9223966D0/en
Application filed by Ici Plc filed Critical Ici Plc
Application granted granted Critical
Publication of TW280815B publication Critical patent/TW280815B/zh

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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
TW083109260A 1992-05-29 1993-05-31 TW280815B (en:Method)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB929211441A GB9211441D0 (en) 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid
GB929223966A GB9223966D0 (en) 1992-11-16 1992-11-16 Filtration method

Publications (1)

Publication Number Publication Date
TW280815B true TW280815B (en:Method) 1996-07-11

Family

ID=26300959

Family Applications (2)

Application Number Title Priority Date Filing Date
TW082104414A TW242617B (en:Method) 1992-05-29 1993-05-31
TW083109260A TW280815B (en:Method) 1992-05-29 1993-05-31

Family Applications Before (1)

Application Number Title Priority Date Filing Date
TW082104414A TW242617B (en:Method) 1992-05-29 1993-05-31

Country Status (12)

Country Link
US (2) US5583254A (en:Method)
EP (1) EP0642490A1 (en:Method)
JP (1) JPH07507291A (en:Method)
CN (1) CN1085889A (en:Method)
AU (1) AU681078B2 (en:Method)
BR (1) BR9306434A (en:Method)
CA (1) CA2136621A1 (en:Method)
GB (1) GB9310070D0 (en:Method)
RU (1) RU94046088A (en:Method)
SG (1) SG52279A1 (en:Method)
TW (2) TW242617B (en:Method)
WO (1) WO1993024440A1 (en:Method)

Families Citing this family (101)

* Cited by examiner, † Cited by third party
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US5602187A (en) * 1992-05-18 1997-02-11 Swig Pty Ltd. Polyethylene terephthalate decontamination
US5504121A (en) * 1992-05-18 1996-04-02 Swig Pty Ltd. Polyethylene terephthalate decontamination
GB9310070D0 (en) * 1992-05-29 1993-06-30 Ici Plc Process for the production of purified terephthalic acid
GB9400570D0 (en) * 1994-01-13 1994-03-09 Ici Plc Handling of materials at elevated pressure
US5470473A (en) * 1994-02-17 1995-11-28 Baker Hughes Incorporated Rotary vacuum filtration drum with valved hopper cake treatment means
TW299318B (en:Method) * 1994-11-15 1997-03-01 Mitsubishi Chem Corp
KR100431684B1 (ko) * 1995-06-05 2004-08-16 이.아이,듀우판드네모아앤드캄파니 유출가스처리방법
US5961942A (en) * 1995-06-05 1999-10-05 E. I. Du Pont De Nemours And Company Effluent gas treatment
TW442461B (en) * 1996-02-22 2001-06-23 Du Pont Process for the production of an aromatic carboxylic acid
KR100463612B1 (ko) * 1996-02-22 2005-02-28 이.아이,듀우판드네모아앤드캄파니 방향족폴리카르복실산의제조방법
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KR19990072006A (ko) * 1996-10-30 1999-09-27 나까니시 히로유끼 방향족디카르복실산의제조방법
GB9705349D0 (en) 1997-03-14 1997-04-30 Ici Plc Treatment of effluent streams
US6194609B1 (en) 1997-06-30 2001-02-27 Bp Amoco Corporation Crystallization in a plate heat exchanger
WO1999000167A1 (en) * 1997-06-30 1999-01-07 Bp Amoco Corporation Crystallization in a plate heat exchanger
GB9717251D0 (en) * 1997-08-15 1997-10-22 Ici Plc Process and apparatus
IT1311976B1 (it) * 1999-03-25 2002-03-22 Franco Codignola Procedimento per la produzione di acidi aromatici.
IT1319169B1 (it) 2000-07-14 2003-09-26 Eurotecnica Dev & Licensing Sr Procedimento per la purificazione di acidi carbossilici aromatici.
US6689903B2 (en) 2001-06-04 2004-02-10 Eastman Chemical Company Crystallization method for production of purified aromatic dicarboxylic acids
US7485747B2 (en) * 2001-06-04 2009-02-03 Eastman Chemical Company Two stage oxidation process for the production of aromatic dicarboxylic acids
US7196215B2 (en) 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
US7276625B2 (en) 2002-10-15 2007-10-02 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
WO2004043893A1 (ja) * 2002-11-14 2004-05-27 Mitsubishi Chemical Corporation テレフタル酸の製造方法
US7132566B2 (en) 2003-09-22 2006-11-07 Eastman Chemical Company Process for the purification of a crude carboxylic acid slurry
US7074954B2 (en) * 2002-12-09 2006-07-11 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
BR0316462A (pt) 2002-12-09 2005-10-11 Eastman Chem Co Processos para reduzir uma suspensão de ácido carboxìlico purificado, para purificar um produto de oxidação em estágios, para produzir um produto de ácido carboxìlico purificado, e, suspensão de ácido carboxìlico purificado
US7161027B2 (en) 2002-12-09 2007-01-09 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
BR0317963A (pt) * 2003-01-10 2005-11-29 Mitsubishi Chem Corp Método de separação centrìfuga da lama contendo ácido carboxìlico aromático
US7193109B2 (en) 2003-03-06 2007-03-20 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
US20040215036A1 (en) * 2003-04-25 2004-10-28 Robert Lin Method for heating a crude carboxylic acid slurry in a post oxidation zone by the addition of steam
US20050059709A1 (en) * 2003-09-15 2005-03-17 Meythaler Jay M. Treatment of a neuropathy with rapid release aminopyridine
US7214760B2 (en) * 2004-01-15 2007-05-08 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
US7546747B2 (en) 2004-01-15 2009-06-16 Eastman Chemical Company Process for production of a dried carboxylic acid cake suitable for use in polyester production
US20050256335A1 (en) * 2004-05-12 2005-11-17 Ovidiu Marin Providing gases to aromatic carboxylic acid manufacturing processes
KR100883288B1 (ko) 2004-05-28 2009-02-11 미쓰비시 가가꾸 가부시키가이샤 고순도 테레프탈산의 제조 방법
WO2005115956A1 (ja) * 2004-05-28 2005-12-08 Mitsubishi Chemical Corporation 高純度テレフタル酸の製造方法
WO2006001449A1 (ja) * 2004-06-28 2006-01-05 Mitsubishi Chemical Corporation 高純度テレフタル酸の製造方法
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 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
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 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
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US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 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
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
ES2278267T3 (es) * 2004-12-15 2007-08-01 Saudi Basic Industries Corporation Proceso para preparar acido tereftalico purificado.
KR100708919B1 (ko) 2005-05-30 2007-04-17 삼성석유화학(주) 테레프탈산의 회수 방법
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7358389B2 (en) 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US20070179312A1 (en) * 2006-02-02 2007-08-02 O'meadhra Ruairi Seosamh Process for the purification of a crude carboxylic axid slurry
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
US7863483B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Carboxylic acid production process
US8173836B2 (en) * 2006-03-01 2012-05-08 Grupo Petrotemex, S.A. De C.V. Method and apparatus for drying carboxylic acid
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
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of 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
US7393973B2 (en) * 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US7847121B2 (en) * 2006-03-01 2010-12-07 Eastman Chemical Company Carboxylic acid production process
US20070208199A1 (en) * 2006-03-01 2007-09-06 Kenny Randolph Parker Methods and apparatus for isolating carboxylic acid
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7462736B2 (en) * 2006-03-01 2008-12-09 Eastman Chemical Company Methods and apparatus for isolating carboxylic acid
US7420082B2 (en) 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
KR101827229B1 (ko) * 2007-05-31 2018-02-07 다우 이탈리아 에스.알.엘. 테레프탈산의 회수를 위한 개선된 방법
RU2463096C2 (ru) * 2007-12-20 2012-10-10 Хитачи Плант Текнолоджиз, Лтд. Способ фильтрации кристаллической суспензии
CN101903072B (zh) * 2007-12-20 2013-12-25 株式会社日立工业设备技术 结晶浆料的过滤方法
US8614350B2 (en) 2008-01-15 2013-12-24 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8455680B2 (en) 2008-01-15 2013-06-04 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
WO2010049697A2 (en) * 2008-10-31 2010-05-06 Invista Technologies S.A.R.L. Improved pure carboxylic acid filtration
WO2010119484A1 (ja) * 2009-04-16 2010-10-21 株式会社日立プラントテクノロジー 晶析スラリーからの結晶の回収方法
CN102126945A (zh) * 2010-01-13 2011-07-20 中国石油化工股份有限公司 回收精对苯二甲酸的方法
EP2585430B1 (en) * 2010-06-28 2019-04-17 Johnson Matthey Davy Technologies Limited Process and system for the separation of carboxylic acids (such as terephthalic acid) from a slurry
JP5802115B2 (ja) * 2011-11-18 2015-10-28 株式会社日立製作所 粗製テレフタル酸の精製方法
CN102626646B (zh) * 2012-04-13 2014-04-02 大连华峰发展公司 一种氧化段钴锰催化剂回收利用装置及其方法
CN103936581A (zh) * 2014-04-24 2014-07-23 天华化工机械及自动化研究设计院有限公司 一种提高cta溶剂交换效率的方法
EP3297996B1 (en) 2015-05-21 2019-07-10 Avantium Knowledge Centre B.V. Process for the purification of a carboxylic acid-containing composition
EP3297995B1 (en) 2015-05-21 2019-07-10 Avantium Knowledge Centre B.V. Process for the preparation of an aromatic dicarboxylic acid
EP3545121B1 (en) 2016-11-24 2021-06-09 Avantium Knowledge Centre B.v. Process for treating a dicarboxylic acid composition
WO2020006446A1 (en) * 2018-06-29 2020-01-02 Bp Corporation North America Inc. Solid-liquid separation processes using a large pore filter
CN110117244A (zh) * 2019-05-27 2019-08-13 太仓塑料助剂厂有限公司 过氧化二异丙苯的洗涤结晶方法
EP4021881B1 (en) * 2019-08-28 2023-05-10 Koch Technology Solutions UK Limited Apparatus for purifying terephthalic acid
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US5175355A (en) * 1991-04-12 1992-12-29 Amoco Corporation Improved process for recovery of purified terephthalic acid
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GB9310070D0 (en) * 1992-05-29 1993-06-30 Ici Plc Process for the production of purified terephthalic acid

Also Published As

Publication number Publication date
RU94046088A (ru) 1996-09-27
TW242617B (en:Method) 1995-03-11
CN1085889A (zh) 1994-04-27
CA2136621A1 (en) 1993-12-09
SG52279A1 (en) 1998-09-28
US5698734A (en) 1997-12-16
EP0642490A1 (en) 1995-03-15
US5583254A (en) 1996-12-10
BR9306434A (pt) 1998-09-15
JPH07507291A (ja) 1995-08-10
WO1993024440A1 (en) 1993-12-09
AU681078B2 (en) 1997-08-21
GB9310070D0 (en) 1993-06-30
AU4081593A (en) 1993-12-30

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