GB1555246A - Secondary oxidation of fluid effluent from primary oxidation of meta- or paraxylene - Google Patents

Secondary oxidation of fluid effluent from primary oxidation of meta- or paraxylene

Info

Publication number
GB1555246A
GB1555246A GB4400676A GB4400676A GB1555246A GB 1555246 A GB1555246 A GB 1555246A GB 4400676 A GB4400676 A GB 4400676A GB 4400676 A GB4400676 A GB 4400676A GB 1555246 A GB1555246 A GB 1555246A
Authority
GB
United Kingdom
Prior art keywords
oxidation
paraxylene
meta
fluid effluent
primary
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
Application number
GB4400676A
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.)
Standard Oil Co
Original Assignee
Standard Oil Co
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 Standard Oil Co filed Critical Standard Oil Co
Publication of GB1555246A publication Critical patent/GB1555246A/en
Expired 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
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265—Preparation 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
GB4400676A 1975-10-24 1976-10-22 Secondary oxidation of fluid effluent from primary oxidation of meta- or paraxylene Expired GB1555246A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US62567575A 1975-10-24 1975-10-24

Publications (1)

Publication Number Publication Date
GB1555246A true GB1555246A (en) 1979-11-07

Family

ID=24507104

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4400676A Expired GB1555246A (en) 1975-10-24 1976-10-22 Secondary oxidation of fluid effluent from primary oxidation of meta- or paraxylene

Country Status (11)

Country Link
JP (1) JPS6048497B2 (enrdf_load_stackoverflow)
BE (1) BE847474A (enrdf_load_stackoverflow)
CA (1) CA1062279A (enrdf_load_stackoverflow)
DE (1) DE2647698A1 (enrdf_load_stackoverflow)
DK (1) DK159259C (enrdf_load_stackoverflow)
FR (1) FR2328688A1 (enrdf_load_stackoverflow)
GB (1) GB1555246A (enrdf_load_stackoverflow)
IT (1) IT1073924B (enrdf_load_stackoverflow)
LU (1) LU76048A1 (enrdf_load_stackoverflow)
NL (1) NL188637C (enrdf_load_stackoverflow)
YU (1) YU42274B (enrdf_load_stackoverflow)

Cited By (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3209069A1 (de) * 1981-03-16 1982-11-18 Labofina S.A., 1040 Bruxelles Verfahren zur herstellung von terephthalsaeure
EP0465100A1 (en) * 1990-06-25 1992-01-08 Mitsubishi Gas Chemical Company, Inc. Process for producing high purity isophthalic acid
US5189209A (en) * 1990-05-17 1993-02-23 Mitsubishi Gas Chemical Company, Inc. Process for producing highly pure isophthalic acid
WO2006028755A1 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028818A1 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Crude terephthalic acid composition and production process thereof
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
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 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
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7659427B2 (en) 2004-09-02 2010-02-09 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
WO2019005532A1 (en) * 2017-06-29 2019-01-03 Bp Corporation North America Inc. METHODS OF MAKING AROMATIC CARBOXYLIC ACIDS
CN112110813A (zh) * 2020-09-18 2020-12-22 中国石化扬子石油化工有限公司 一种促进偏苯三甲酸结晶的方法

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2714985C2 (de) * 1977-04-04 1982-05-06 Chemische Werke Hüls AG, 4370 Marl Verfahren zur Reinigung von Terephthalsäure
JPS5470235A (en) * 1977-11-14 1979-06-05 Mitsubishi Chem Ind Ltd Preparation of terephthalic acid
DE3128147C2 (de) * 1981-07-16 1986-03-06 Dynamit Nobel Ag, 5210 Troisdorf Verfahren zur Gewinnung von aromatischen Monocarbonsäuren
US5183933A (en) * 1991-10-15 1993-02-02 Amoco Corporation Process for preparing 2,6-naphthalene-dicarboxylic acid

Cited By (49)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3209069A1 (de) * 1981-03-16 1982-11-18 Labofina S.A., 1040 Bruxelles Verfahren zur herstellung von terephthalsaeure
US5189209A (en) * 1990-05-17 1993-02-23 Mitsubishi Gas Chemical Company, Inc. Process for producing highly pure isophthalic acid
EP0465100A1 (en) * 1990-06-25 1992-01-08 Mitsubishi Gas Chemical Company, Inc. Process for producing high purity isophthalic acid
US5132450A (en) * 1990-06-25 1992-07-21 Mitsubishi Gas Chemical Company, Inc. Process for producing high purity isophthalic acid
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US8470257B2 (en) 2004-09-02 2013-06-25 Grupo Petrotemex, S.A. De C.V. Optimized liquid-phase oxidation
US8178054B2 (en) 2004-09-02 2012-05-15 Grupo Petrotemex, S. A. DE C. V. Optimized liquid-phase oxidation
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US8114356B2 (en) 2004-09-02 2012-02-14 Grupo Pretrotemex, S.A. de C.V. Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7498003B2 (en) 2004-09-02 2009-03-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7977505B2 (en) 2004-09-02 2011-07-12 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028755A1 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028818A1 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Crude terephthalic acid composition and production process thereof
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7498002B2 (en) 2004-09-02 2009-03-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7659427B2 (en) 2004-09-02 2010-02-09 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7960581B2 (en) 2004-09-02 2011-06-14 Grupo Petrotemex, S.A. De C.V. Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 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
EP2251315A1 (en) * 2004-09-02 2010-11-17 Eastman Chemical Company Crude therephthalic acid composition and production process thereof
US7910071B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7902396B2 (en) * 2004-09-02 2011-03-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7901636B2 (en) 2004-09-02 2011-03-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US8501986B2 (en) * 2004-11-29 2013-08-06 Grupo Petrotemex, S.A. De C.V. Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7491369B2 (en) 2006-01-04 2009-02-17 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
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
WO2019005532A1 (en) * 2017-06-29 2019-01-03 Bp Corporation North America Inc. METHODS OF MAKING AROMATIC CARBOXYLIC ACIDS
CN110944972A (zh) * 2017-06-29 2020-03-31 Bp北美公司 制造芳族羧酸的方法
US10843995B2 (en) 2017-06-29 2020-11-24 Bp Corporation North America Inc. Processes for manufacturing aromatic carboxylic acids
CN112110813A (zh) * 2020-09-18 2020-12-22 中国石化扬子石油化工有限公司 一种促进偏苯三甲酸结晶的方法

Also Published As

Publication number Publication date
FR2328688A1 (fr) 1977-05-20
NL188637C (nl) 1992-08-17
YU260576A (en) 1982-05-31
YU42274B (en) 1988-08-31
LU76048A1 (enrdf_load_stackoverflow) 1977-05-31
NL7611720A (nl) 1977-04-26
BE847474A (fr) 1977-04-20
DE2647698C2 (enrdf_load_stackoverflow) 1989-06-15
JPS5285136A (en) 1977-07-15
DE2647698A1 (de) 1977-04-28
IT1073924B (it) 1985-04-17
FR2328688B1 (enrdf_load_stackoverflow) 1978-12-15
CA1062279A (en) 1979-09-11
DK477776A (da) 1977-04-25
DK159259B (da) 1990-09-24
JPS6048497B2 (ja) 1985-10-28
DK159259C (da) 1991-04-08

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Legal Events

Date Code Title Description
PS Patent sealed
PE20 Patent expired after termination of 20 years

Effective date: 19961021