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BR9907865A - Processo contìnuo para preparar ácido carboxìlico aromático por oxidação em fase lìquida de uma carga aromática - Google Patents

Processo contìnuo para preparar ácido carboxìlico aromático por oxidação em fase lìquida de uma carga aromática

Info

Publication number
BR9907865A
BR9907865A BR9907865-1A BR9907865A BR9907865A BR 9907865 A BR9907865 A BR 9907865A BR 9907865 A BR9907865 A BR 9907865A BR 9907865 A BR9907865 A BR 9907865A
Authority
BR
Brazil
Prior art keywords
aromatic
liquid phase
carboxylic acid
continuous process
aromatic carboxylic
Prior art date
Application number
BR9907865-1A
Other languages
English (en)
Inventor
Jeffrey L Broeker
Frank G Belmont
Thomas M Bartos
Alakananda Bhattacharyya
Anne M Karachewski
Bruce I Rosen
Kenneth J Abrams
Original Assignee
Bp Amoco 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 Bp Amoco Corp filed Critical Bp Amoco Corp
Publication of BR9907865A publication Critical patent/BR9907865A/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/09—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
    • C07C29/12—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of esters of mineral acids
    • C07C29/124—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of esters of mineral acids of halides
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00—Halogens; Halogen acids
    • C01B7/09—Bromine; Hydrogen bromide
    • C01B7/093—Hydrogen bromide
    • 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
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

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

Abstract

"PROCESSO CONTìNUO PARA PREPARAR áCIDO CARBOXìLICO AROMáTICO POR OXIDAçãO EM FASE LìQUIDA DE UMA CARGA AROMáTICA''.. Processos são descritos para recuperação de brometo de hidrogênio a partir de um ou mais compostos de brometo de alquila pela hidrólise dos compostos de brometo de alquila para brometo de hidrogênio e álcoois correspondentes, e simultaneamente separação pelo menos dos produtos alcoólicos de hidrólise do componente de solvente de ácido monocarboxílico alifático. Também são descritos processos para preparar ácidos carboxílicos aromáticos pela oxidação exotérmica em fase líquida de um composto de alimentação aromático em que a energia produzida pela oxidação exotérmica é eficientemente recuperada
BR9907865-1A 1998-02-11 1999-02-08 Processo contìnuo para preparar ácido carboxìlico aromático por oxidação em fase lìquida de uma carga aromática BR9907865A (pt)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US7437198P 1998-02-11 1998-02-11
US09/245,214 US6137001A (en) 1998-02-11 1999-02-05 Process for preparing aromatic carboxylic acids with efficient treatments of gaseous effluent
PCT/US1999/002619 WO1999041221A1 (en) 1998-02-11 1999-02-08 Process for preparing aromatic carboxylic acids with efficient treatments of gaseous effluent

Publications (1)

Publication Number Publication Date
BR9907865A true BR9907865A (pt) 2000-10-24

Family

ID=26755577

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9907865-1A BR9907865A (pt) 1998-02-11 1999-02-08 Processo contìnuo para preparar ácido carboxìlico aromático por oxidação em fase lìquida de uma carga aromática

Country Status (8)

Country Link
US (1) US6137001A (pt)
EP (1) EP1054855A1 (pt)
KR (1) KR20010074427A (pt)
CN (1) CN1290243A (pt)
AU (1) AU750473B2 (pt)
BR (1) BR9907865A (pt)
CA (1) CA2320206A1 (pt)
WO (1) WO1999041221A1 (pt)

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US20080161598A1 (en) * 2004-09-02 2008-07-03 Eastman Chemical Company Optimized Production of Aromatic Dicarboxylic Acids
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US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7880032B2 (en) * 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7501537B2 (en) * 2006-03-01 2009-03-10 Eastman Chemical Company Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US20070203359A1 (en) * 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US7420082B2 (en) * 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7393973B2 (en) * 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US7863481B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US20080179247A1 (en) * 2007-01-30 2008-07-31 Eastman Chemical Company Elimination of Wastewater Treatment System
US9493388B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with direct fired off-gas heating
US9505692B2 (en) * 2008-10-31 2016-11-29 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with self-fuel oxidative destruction
US20100113735A1 (en) * 2008-10-31 2010-05-06 Eastman Chemical Company Integrated Co-Production of Dicarboxylic Acids
US9493387B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with minimal wastewater generation
US9493389B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with enhanced energy recovery
US8884054B2 (en) 2010-06-30 2014-11-11 Uop Llc Process for oxidizing alkyl aromatic compounds
US8884055B2 (en) 2010-06-30 2014-11-11 Uop Llc Process for producing terephthalic acid
US8933266B2 (en) 2010-06-30 2015-01-13 Uop Llc Process for producing terephthalic acid
US8835678B2 (en) 2010-06-30 2014-09-16 Uop Llc Solid terephthalic acid composition
US8754254B2 (en) 2010-06-30 2014-06-17 Uop Llc Process for purifying terephthalic acid
US9045407B2 (en) 2010-06-30 2015-06-02 Uop Llc Mixtures used in oxidizing alkyl aromatic compounds
US8933265B2 (en) 2010-06-30 2015-01-13 Uop Llc Process for oxidizing alkyl aromatic compounds
EP3089957B1 (en) 2013-12-30 2020-12-30 BP Corporation North America Inc. Purification of aromatic carboxylic acids
CN105873889A (zh) 2013-12-30 2016-08-17 Bp北美公司 使用脱水塔冷凝物来纯化粗产物而制备对苯二甲酸的方法
CA2934279A1 (en) 2013-12-31 2015-07-09 Bp Corporation North America Inc. Solid-liquid separations with a no-dry rotary pressure filter
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
US9394223B2 (en) 2013-12-31 2016-07-19 Bp Corporation North America Inc. Oxidation process for preparing purified aromatic carboxylic acids
EP3397610B1 (en) 2015-12-31 2020-12-02 BP Corporation North America Inc. Process for acetic recovery from aqueous streams
NL2016915B1 (en) * 2016-06-08 2017-12-18 Green Granulation Tech Limited Fluidized bed granulation
TW201823194A (zh) 2016-12-29 2018-07-01 美商Ｂｐ公司北美股份有限公司 經純化的對苯二甲酸(pta)排氣孔蒸汽之利用
TW201823193A (zh) * 2016-12-29 2018-07-01 美商Ｂｐ公司北美股份有限公司 經純化的對苯二甲酸(pta)排氣孔乾燥器蒸氣流出物處理技術
TW201842956A (zh) 2017-04-28 2018-12-16 美商Ｂｐ公司北美股份有限公司 使用加壓濕氣線路以避免於經純化的對苯二甲酸(pta)過濾器及線路的積垢
US10843995B2 (en) 2017-06-29 2020-11-24 Bp Corporation North America Inc. Processes for manufacturing aromatic carboxylic acids
WO2019019012A1 (en) 2017-07-25 2019-01-31 Bp Corporation North America Inc. DELIVERY OF A FILTER RINSE PRODUCT OF A PURIFIED AROMATIC CARBOXYLIC ACID FOR ENERGY OPTIMIZATION
WO2019028097A1 (en) 2017-08-01 2019-02-07 Bp Corporation North America Inc. METHOD FOR PREHEATING WATER OF BOILER SUPPLY IN THE MANUFACTURE OF PURIFIED AROMATIC CARBOXYLIC ACIDS
US10703700B2 (en) 2017-08-24 2020-07-07 Uop Llc Liquid phase oxidation of lower alkanes to oxygenates
WO2020006446A1 (en) 2018-06-29 2020-01-02 Bp Corporation North America Inc. Solid-liquid separation processes using a large pore filter
CN109173310A (zh) * 2018-08-29 2019-01-11 张家港市科华化工装备制造有限公司 甲缩醛精馏塔
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EP4051658B1 (en) 2019-10-31 2024-09-04 Ineos Us Chemicals Company Solid-liquid separation processes

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US4966611A (en) * 1989-03-22 1990-10-30 Custom Engineered Materials Inc. Removal and destruction of volatile organic compounds from gas streams
DE69107943T2 (de) * 1990-09-25 1995-07-13 Inst Francais Du Petrol Verfahren zur Herstellung von Boroxid durch Hydrolyse von Methylborat und seine Anwendung bei der Oxidation von gesättigten Kohlenwasserstoffen zu Alkoholen.
US5102505A (en) * 1990-11-09 1992-04-07 Union Carbide Chemicals & Plastics Technology Corporation Mixed aldehyde product separation by distillation
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Also Published As

Publication number Publication date
WO1999041221A1 (en) 1999-08-19
AU2590499A (en) 1999-08-30
CN1290243A (zh) 2001-04-04
AU750473B2 (en) 2002-07-18
US6137001A (en) 2000-10-24
KR20010074427A (ko) 2001-08-04
EP1054855A1 (en) 2000-11-29
CA2320206A1 (en) 1999-08-19

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Legal Events

Date Code Title Description
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE 5A, 6A, 7A E 8A ANUIDADES.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1910 DE 14/08/2007.