RU94046087A - Способ производства очищенной терефталевой кислоты и устройство инжекции водяного пара, используемое в способе производства очищенной терефталевой кислоты - Google Patents

Способ производства очищенной терефталевой кислоты и устройство инжекции водяного пара, используемое в способе производства очищенной терефталевой кислоты

Info

Publication number
RU94046087A
RU94046087A RU94046087/04A RU94046087A RU94046087A RU 94046087 A RU94046087 A RU 94046087A RU 94046087/04 A RU94046087/04 A RU 94046087/04A RU 94046087 A RU94046087 A RU 94046087A RU 94046087 A RU94046087 A RU 94046087A
Authority
RU
Russia
Prior art keywords
terephthalic acid
mixture
water
purified terephthalic
acid production
Prior art date
Application number
RU94046087/04A
Other languages
English (en)
Russian (ru)
Inventor
Артур Тернер Джон
Gb]
Хиндмарш Эрик
Паркер Дэвид
Питер Майлн Ян
Original Assignee
Империал Кемикал Индастриз П Л С. (GB)
Империал Кемикал Индастриз П Л С.
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 Империал Кемикал Индастриз П Л С. (GB), Империал Кемикал Индастриз П Л С. filed Critical Империал Кемикал Индастриз П Л С. (GB)
Publication of RU94046087A publication Critical patent/RU94046087A/ru

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)
RU94046087/04A 1992-05-29 1993-05-20 Способ производства очищенной терефталевой кислоты и устройство инжекции водяного пара, используемое в способе производства очищенной терефталевой кислоты RU94046087A (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9211415.6 1992-05-29
GB929211415A GB9211415D0 (en) 1992-05-29 1992-05-29 Process for the production of purified terephthalic acid

Publications (1)

Publication Number Publication Date
RU94046087A true RU94046087A (ru) 1996-09-27

Family

ID=10716228

Family Applications (1)

Application Number Title Priority Date Filing Date
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

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)

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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

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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
GB9211415D0 (en) 1992-07-15
DE69325905D1 (de) 1999-09-09
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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