GB9211415D0 - Process for the production of purified terephthalic acid - Google Patents

Process for the production of purified terephthalic acid

Info

Publication number
GB9211415D0
GB9211415D0 GB929211415A GB9211415A GB9211415D0 GB 9211415 D0 GB9211415 D0 GB 9211415D0 GB 929211415 A GB929211415 A GB 929211415A GB 9211415 A GB9211415 A GB 9211415A GB 9211415 D0 GB9211415 D0 GB 9211415D0
Authority
GB
United Kingdom
Prior art keywords
cta
mixture
aqueous
terephthalic acid
production
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.)
Pending
Application number
GB929211415A
Other languages
English (en)
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.)
Imperial Chemical Industries Ltd
Original Assignee
Imperial Chemical Industries Ltd
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 Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Priority to GB929211415A priority Critical patent/GB9211415D0/en
Publication of GB9211415D0 publication Critical patent/GB9211415D0/en
Priority to GB939310094A priority patent/GB9310094D0/en
Priority to RU94046087/04A priority patent/RU94046087A/ru
Priority to PCT/GB1993/001033 priority patent/WO1993024441A1/en
Priority to DE69325905T priority patent/DE69325905T2/de
Priority to EP93910240A priority patent/EP0642491B1/en
Priority to BR9306418A priority patent/BR9306418A/pt
Priority to AU40825/93A priority patent/AU668725B2/en
Priority to IN521DE1993 priority patent/IN186258B/en
Priority to CA002134873A priority patent/CA2134873A1/en
Priority to ES93910240T priority patent/ES2136661T3/es
Priority to AT93910240T priority patent/ATE182877T1/de
Priority to JP6500293A priority patent/JPH07507292A/ja
Priority to ZA933572A priority patent/ZA933572B/xx
Priority to EG33193A priority patent/EG20633A/xx
Priority to MX9303172A priority patent/MX9303172A/es
Priority to CN93108224A priority patent/CN1039315C/zh
Pending 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
    • C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
GB929211415A 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid Pending GB9211415D0 (en)

Priority Applications (17)

Application Number Priority Date Filing Date Title
GB929211415A GB9211415D0 (en) 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid
GB939310094A GB9310094D0 (en) 1992-05-29 1993-05-17 Process for the production of purified terephthalic acid
JP6500293A JPH07507292A (ja) 1992-05-29 1993-05-20 精製テレフタル酸の製造方法
IN521DE1993 IN186258B (cg-RX-API-DMAC7.html) 1992-05-29 1993-05-20
CA002134873A CA2134873A1 (en) 1992-05-29 1993-05-20 Process for the production of purified terephthalic acid
DE69325905T DE69325905T2 (de) 1992-05-29 1993-05-20 Verfahren zur herstellung von gereinigter terphthalsäure
EP93910240A EP0642491B1 (en) 1992-05-29 1993-05-20 Process for the production of purified terephthalic acid
BR9306418A BR9306418A (pt) 1992-05-29 1993-05-20 Processo para a produção de ácido tereftálico purificado e dispositivo de injeção de vapor para realizar a mistura íntima da corrente deste processo com o vapor quente
AU40825/93A AU668725B2 (en) 1992-05-29 1993-05-20 Process for the production of purified terephthalic acid
RU94046087/04A RU94046087A (ru) 1992-05-29 1993-05-20 Способ производства очищенной терефталевой кислоты и устройство инжекции водяного пара, используемое в способе производства очищенной терефталевой кислоты
PCT/GB1993/001033 WO1993024441A1 (en) 1992-05-29 1993-05-20 Process for the production of purified terephthalic acid
ES93910240T ES2136661T3 (es) 1992-05-29 1993-05-20 Procedimiento de produccion de acido tereftalico purificado.
AT93910240T ATE182877T1 (de) 1992-05-29 1993-05-20 Verfahren zur herstellung von gereinigter terphthalsäure
ZA933572A ZA933572B (en) 1992-05-29 1993-05-21 Process for the production of purified terephthalic acid
EG33193A EG20633A (en) 1992-05-29 1993-05-26 Process for the production of purified terephthalic acid
MX9303172A MX9303172A (es) 1992-05-29 1993-05-28 Procedimiento para la produccion de acido tereftalico purificado.
CN93108224A CN1039315C (zh) 1992-05-29 1993-05-29 纯对苯二酸的制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB929211415A GB9211415D0 (en) 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid

Publications (1)

Publication Number Publication Date
GB9211415D0 true GB9211415D0 (en) 1992-07-15

Family

ID=10716228

Family Applications (2)

Application Number Title Priority Date Filing Date
GB929211415A Pending GB9211415D0 (en) 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid
GB939310094A Pending GB9310094D0 (en) 1992-05-29 1993-05-17 Process for the production of purified terephthalic acid

Family Applications After (1)

Application Number Title Priority Date Filing Date
GB939310094A Pending GB9310094D0 (en) 1992-05-29 1993-05-17 Process for the production of purified terephthalic acid

Country Status (14)

Country Link
EP (1) EP0642491B1 (cg-RX-API-DMAC7.html)
JP (1) JPH07507292A (cg-RX-API-DMAC7.html)
CN (1) CN1039315C (cg-RX-API-DMAC7.html)
AT (1) ATE182877T1 (cg-RX-API-DMAC7.html)
AU (1) AU668725B2 (cg-RX-API-DMAC7.html)
BR (1) BR9306418A (cg-RX-API-DMAC7.html)
CA (1) CA2134873A1 (cg-RX-API-DMAC7.html)
DE (1) DE69325905T2 (cg-RX-API-DMAC7.html)
ES (1) ES2136661T3 (cg-RX-API-DMAC7.html)
GB (2) GB9211415D0 (cg-RX-API-DMAC7.html)
IN (1) IN186258B (cg-RX-API-DMAC7.html)
RU (1) RU94046087A (cg-RX-API-DMAC7.html)
WO (1) WO1993024441A1 (cg-RX-API-DMAC7.html)
ZA (1) ZA933572B (cg-RX-API-DMAC7.html)

Families Citing this family (64)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5504121A (en) * 1992-05-18 1996-04-02 Swig Pty Ltd. Polyethylene terephthalate decontamination
US5602187A (en) * 1992-05-18 1997-02-11 Swig Pty Ltd. Polyethylene terephthalate decontamination
US5922775A (en) * 1997-10-23 1999-07-13 Octamer, Inc. Method of treating malignant tumors with ketone thyroxine analogues having no significant hormonal activity
WO2004063136A1 (ja) * 2003-01-08 2004-07-29 Mitsubishi Chemical Corporation 高純度テレフタル酸の製造方法
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
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
US7351396B2 (en) 2003-06-05 2008-04-01 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
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
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
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
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US20080161598A1 (en) 2004-09-02 2008-07-03 Eastman Chemical Company Optimized Production of Aromatic Dicarboxylic Acids
US7381836B2 (en) 2004-09-02 2008-06-03 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
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
IN2015DN00761A (cg-RX-API-DMAC7.html) * 2004-09-02 2015-07-10 Grupo Petrotemex Sa De Cv
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7888530B2 (en) 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US20070238899A9 (en) 2004-09-02 2007-10-11 Robert Lin Optimized production of aromatic dicarboxylic acids
EP1786550A2 (en) * 2004-09-02 2007-05-23 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7291270B2 (en) 2004-10-28 2007-11-06 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7273559B2 (en) 2004-10-28 2007-09-25 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7834208B2 (en) 2005-05-19 2010-11-16 Eastman Chemical Company Process to produce a post catalyst removal composition
US7880031B2 (en) 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
US7897809B2 (en) 2005-05-19 2011-03-01 Eastman Chemical Company Process to produce an enrichment feed
US7919652B2 (en) 2005-05-19 2011-04-05 Eastman Chemical Company Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone
US7557243B2 (en) 2005-05-19 2009-07-07 Eastman Chemical Company Enriched terephthalic acid composition
US7884231B2 (en) 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
US7304178B2 (en) 2005-05-19 2007-12-04 Eastman Chemical Company Enriched isophthalic acid composition
US7741516B2 (en) 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US7432395B2 (en) 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
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
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
US20070203359A1 (en) 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US7897808B2 (en) 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7863481B2 (en) 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US7888529B2 (en) 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US7880032B2 (en) 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US9199905B2 (en) * 2008-10-31 2015-12-01 Invista North America S.A.R.L. Pure carboxylic acid filtration
GB201016049D0 (en) 2010-09-24 2010-11-10 Davy Process Techn Ltd Process and system
CN103121940B (zh) * 2011-11-18 2015-11-18 中国石油化工股份有限公司 加氢处理粗间苯二甲酸方法
DE102012007675A1 (de) * 2012-04-17 2013-10-17 BOKELA Ingenieurgesellschaft für mechanische Verfahrenstechnik mbH Verfahren und Anlage zum Herstellen von TA(Terephtalsäure)
KR102185028B1 (ko) 2013-12-30 2020-12-01 비피 코포레이션 노쓰 아메리카 인코포레이티드 방향족 카르복실산의 정제
JP6564381B2 (ja) 2013-12-31 2019-08-21 ビーピー・コーポレーション・ノース・アメリカ・インコーポレーテッド 精製芳香族カルボン酸の製造における高圧の凝縮物の生成

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3522298A (en) * 1966-03-30 1970-07-28 Mobil Oil Corp Terephthalic acid purification process
DE2601431A1 (de) * 1976-01-16 1977-07-21 Wiegand Karlsruhe Gmbh Direkt-dampf-injektionsgeraet
US4405809A (en) * 1981-12-04 1983-09-20 Standard Oil Company (Indiana) Process for the manufacture of aromatic polycarboxylic acids having delta Y values below ten
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

Also Published As

Publication number Publication date
ZA933572B (en) 1994-02-14
DE69325905T2 (de) 2000-03-30
WO1993024441A1 (en) 1993-12-09
CN1039315C (zh) 1998-07-29
JPH07507292A (ja) 1995-08-10
AU4082593A (en) 1993-12-30
CA2134873A1 (en) 1993-12-09
GB9310094D0 (en) 1993-06-30
ES2136661T3 (es) 1999-12-01
DE69325905D1 (de) 1999-09-09
RU94046087A (ru) 1996-09-27
EP0642491B1 (en) 1999-08-04
EP0642491A1 (en) 1995-03-15
IN186258B (cg-RX-API-DMAC7.html) 2001-07-21
BR9306418A (pt) 1998-09-15
AU668725B2 (en) 1996-05-16
CN1085891A (zh) 1994-04-27
ATE182877T1 (de) 1999-08-15

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