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AR020637A1 - Un proceso para la produccion de acido tereftalico y/o dimetiltereftalato - Google Patents

Un proceso para la produccion de acido tereftalico y/o dimetiltereftalato

Info

Publication number
AR020637A1
AR020637A1 ARP990103687A ARP990103687A AR020637A1 AR 020637 A1 AR020637 A1 AR 020637A1 AR P990103687 A ARP990103687 A AR P990103687A AR P990103687 A ARP990103687 A AR P990103687A AR 020637 A1 AR020637 A1 AR 020637A1
Authority
AR
Argentina
Prior art keywords
xylene
catalyst
ortho
para
terephthalic acid
Prior art date
Application number
ARP990103687A
Other languages
English (en)
Original Assignee
Mobil Oil Corp
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 Mobil Oil Corp filed Critical Mobil Oil Corp
Publication of AR020637A1 publication Critical patent/AR020637A1/es

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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
    • C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
    • C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
    • C07C6/123—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of only one hydrocarbon
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/39—Preparation of carboxylic acid esters by oxidation of groups which are precursors for the acid moiety of the ester
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Un proceso para producir ácido tereftálico y/o dimetil tereftalato que incluye poner en contacto una corriente de reaccion que contiene tolueno con unprimer catalizador bajo condiciones de desproporcionamiento de tolueno para producir una corriented e producto intermedia de para-xileno con cantidadesnegligibles de orto-xileno. El primer catalizador incluye un tamiz molecular cristalino que tiene un régimen de difusion de orto-xileno de por lo menos50 minutos. El primer catalizador puede sermodi ficado por selectivacion con un compuesto de silicio o un compuesto de carbono. La corriente del productointermedio, sin necesitar purificacion del para-xileno es oxidada para dar ácido tereftálico o dimetiltereftalato.
ARP990103687A 1998-07-28 1999-07-27 Un proceso para la produccion de acido tereftalico y/o dimetiltereftalato AR020637A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/123,281 US6133470A (en) 1998-07-28 1998-07-28 Integration of p-xylene production and subsequent conversion process

Publications (1)

Publication Number Publication Date
AR020637A1 true AR020637A1 (es) 2002-05-22

Family

ID=22407751

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP990103687A AR020637A1 (es) 1998-07-28 1999-07-27 Un proceso para la produccion de acido tereftalico y/o dimetiltereftalato

Country Status (14)

Country Link
US (1) US6133470A (es)
EP (1) EP1100765B1 (es)
JP (1) JP2002521467A (es)
KR (1) KR20010071053A (es)
CN (1) CN1319084A (es)
AR (1) AR020637A1 (es)
AT (1) ATE284859T1 (es)
AU (1) AU5005599A (es)
BR (1) BR9912567A (es)
CA (1) CA2338656A1 (es)
DE (1) DE69922660D1 (es)
TW (1) TW491836B (es)
WO (1) WO2000006530A1 (es)
ZA (1) ZA200100764B (es)

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US6037513A (en) * 1998-07-09 2000-03-14 Mobil Oil Corporation Hydroalkylation of aromatic hydrocarbons
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
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
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
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
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7249469B2 (en) * 2004-11-18 2007-07-31 Exxonmobil Chemical Patents Inc. Method for separating a multicomponent stream
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
WO2009128984A1 (en) * 2008-04-14 2009-10-22 Exxonmobil Chemical Patents Inc. Process for producing cyclohexylbenzene
CN102015589B (zh) * 2008-05-01 2013-05-29 埃克森美孚化学专利公司 用于制备环己基苯的方法
JP5461553B2 (ja) * 2008-07-28 2014-04-02 エクソンモービル・ケミカル・パテンツ・インク Ｅｍｍ−１２を用いるアルキル芳香族化合物の製造方法
CN103833046B (zh) * 2008-07-28 2016-10-05 埃克森美孚化学专利公司 使用emm-13制备烷基芳族化合物的方法
US8519194B2 (en) 2009-02-26 2013-08-27 Exxonmobil Chemical Patents Inc. Process for producing cyclohexylbenzene
WO2012050751A1 (en) 2010-10-11 2012-04-19 Exxonmobil Chemical Patents Inc. Activation and use of hydroalkylation catalysts
US9233887B2 (en) 2010-12-21 2016-01-12 Exxonmobil Chemical Patents Inc. Process for producing a monocycloalkyl-substituted aromatic compound
WO2013058882A1 (en) 2011-10-17 2013-04-25 Exxonmobil Chemical Patents Inc. Process for producing cyclohexylbenzene
US10661258B2 (en) * 2013-06-13 2020-05-26 Exxonmobil Chemical Patents Inc. In-situ trim coke selectivation of toluene disproportionation catalyst
CN120091985A (zh) * 2022-08-03 2025-06-03 伊士曼化工公司 来自废塑料的回收成分对苯二甲酸二甲酯和相关的化学组分

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GB727989A (en) * 1951-04-13 1955-04-13 Imhausen & Co Ges Mit Beschrae Improvements in or relating to the production of benzene polycarboxylic acids or derivatives thereof
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NL120513C (es) * 1959-05-09
US4007231A (en) * 1975-11-24 1977-02-08 Mobil Oil Corporation Selective production of para-xylene
US4029716A (en) * 1975-12-08 1977-06-14 Mobil Oil Corporation Selective production of para-xylene
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US5602066A (en) * 1995-06-29 1997-02-11 Mobil Oil Corporation Method of making a liquid washed selectivated zeolite catalyst

Also Published As

Publication number Publication date
EP1100765B1 (en) 2004-12-15
EP1100765A4 (en) 2002-07-17
EP1100765A1 (en) 2001-05-23
BR9912567A (pt) 2001-05-02
JP2002521467A (ja) 2002-07-16
ZA200100764B (en) 2001-10-22
WO2000006530A1 (en) 2000-02-10
CN1319084A (zh) 2001-10-24
AU5005599A (en) 2000-02-21
KR20010071053A (ko) 2001-07-28
DE69922660D1 (de) 2005-01-20
TW491836B (en) 2002-06-21
CA2338656A1 (en) 2000-02-10
ATE284859T1 (de) 2005-01-15
US6133470A (en) 2000-10-17

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