KR960006666B1 - 고순도 테레프탈산의 제조방법 - Google Patents

고순도 테레프탈산의 제조방법 Download PDF

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Publication number
KR960006666B1
KR960006666B1 KR1019870011524A KR870011524A KR960006666B1 KR 960006666 B1 KR960006666 B1 KR 960006666B1 KR 1019870011524 A KR1019870011524 A KR 1019870011524A KR 870011524 A KR870011524 A KR 870011524A KR 960006666 B1 KR960006666 B1 KR 960006666B1
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KR
South Korea
Prior art keywords
terephthalic acid
acid
cba
high purity
producing high
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 - Fee Related
Application number
KR1019870011524A
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English (en)
Korean (ko)
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KR880005064A (ko
Inventor
시게미 시라끼
겡이찌 미즈노
Original Assignee
미쓰이세끼유 가가꾸 고오교오 가부시기가이샤
다께바야시 쇼오고
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Application filed by 미쓰이세끼유 가가꾸 고오교오 가부시기가이샤, 다께바야시 쇼오고 filed Critical 미쓰이세끼유 가가꾸 고오교오 가부시기가이샤
Publication of KR880005064A publication Critical patent/KR880005064A/ko
Application granted granted Critical
Publication of KR960006666B1 publication Critical patent/KR960006666B1/ko
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Expired - Fee Related legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14Monocyclic dicarboxylic acids
    • 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

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  • 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)
KR1019870011524A 1986-10-20 1987-10-17 고순도 테레프탈산의 제조방법 Expired - Fee Related KR960006666B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP247500 1986-10-20
JP61-247500 1986-10-20
JP61247500A JPH078823B2 (ja) 1986-10-20 1986-10-20 高純度テレフタル酸の製造方法

Publications (2)

Publication Number Publication Date
KR880005064A KR880005064A (ko) 1988-06-27
KR960006666B1 true KR960006666B1 (ko) 1996-05-22

Family

ID=17164390

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019870011524A Expired - Fee Related KR960006666B1 (ko) 1986-10-20 1987-10-17 고순도 테레프탈산의 제조방법

Country Status (7)

Country Link
EP (1) EP0265137B1 (https=)
JP (1) JPH078823B2 (https=)
KR (1) KR960006666B1 (https=)
CN (1) CN1022182C (https=)
CA (1) CA1296742C (https=)
DE (1) DE3788555T2 (https=)
IN (1) IN168544B (https=)

Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4933492A (en) * 1988-10-13 1990-06-12 Amoco Corporation Purification of crude isophthalic acid
DE4300297C2 (de) * 1993-01-08 1998-01-29 Degussa Verfahren zur selektiven katalytischen Hydrierung der Carbonylgruppe von 4-Carboxylbenzaldehyd
KR100264749B1 (ko) * 1997-02-17 2000-09-01 나까니시 히로유끼 고순도 테레프탈산의 제조 방법
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
JP2008511653A (ja) * 2004-09-02 2008-04-17 イーストマン ケミカル カンパニー 芳香族ジカルボン酸の最適化製造
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company 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
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 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
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 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
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028874A2 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
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
JP5031354B2 (ja) * 2006-12-15 2012-09-19 三井化学株式会社 高純度テレフタル酸の製造方法
KR102185028B1 (ko) * 2013-12-30 2020-12-01 비피 코포레이션 노쓰 아메리카 인코포레이티드 방향족 카르복실산의 정제
US9394223B2 (en) * 2013-12-31 2016-07-19 Bp Corporation North America Inc. Oxidation process for preparing purified aromatic carboxylic acids

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3584039A (en) * 1967-08-30 1971-06-08 Standard Oil Co Fiber-grade terephthalic acid by catalytic hydrogen treatment of dissolved impure terephthalic acid
US4476242A (en) * 1981-10-29 1984-10-09 Standard Oil Company (Indiana) Process for preparing palladium on carbon catalysts for purification of crude terephthalic acid
JPS58116439A (ja) * 1981-12-28 1983-07-11 Mitsubishi Gas Chem Co Inc 高純度芳香族ポリカルボン酸の製造法

Also Published As

Publication number Publication date
CN1022182C (zh) 1993-09-22
IN168544B (https=) 1991-04-20
KR880005064A (ko) 1988-06-27
CN87107051A (zh) 1988-05-04
DE3788555D1 (de) 1994-02-03
EP0265137A2 (en) 1988-04-27
CA1296742C (en) 1992-03-03
DE3788555T2 (de) 1994-04-21
EP0265137B1 (en) 1993-12-22
JPS63104941A (ja) 1988-05-10
JPH078823B2 (ja) 1995-02-01
EP0265137A3 (en) 1989-07-26

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