MX2011004215A - Produccion de acido dicarboxilico con destruccion oxidativa auto-alimentable. - Google Patents

Produccion de acido dicarboxilico con destruccion oxidativa auto-alimentable.

Info

Publication number
MX2011004215A
MX2011004215A MX2011004215A MX2011004215A MX2011004215A MX 2011004215 A MX2011004215 A MX 2011004215A MX 2011004215 A MX2011004215 A MX 2011004215A MX 2011004215 A MX2011004215 A MX 2011004215A MX 2011004215 A MX2011004215 A MX 2011004215A
Authority
MX
Mexico
Prior art keywords
gas
tpa
self
oxidation
optionally
Prior art date
Application number
MX2011004215A
Other languages
English (en)
Inventor
Ronald Buford Sheppard
Timothy Alan Upshaw
Alan George Wonders
Raymond Elbert Fogle Iii
Original Assignee
Grupo Petrotemex Sa De Cv
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 Grupo Petrotemex Sa De Cv filed Critical Grupo Petrotemex Sa De Cv
Publication of MX2011004215A publication Critical patent/MX2011004215A/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
    • C07C63/00—Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14—Monocyclic dicarboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00—Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14—Monocyclic dicarboxylic acids
    • C07C63/15—Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00—Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14—Monocyclic dicarboxylic acids
    • C07C63/15—Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
    • C07C63/26—1,4 - Benzenedicarboxylic acid
    • C07C63/28—Salts thereof

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)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

La invención proporciona un contenido de energía mejorado y recuperación de potencia de eje a partir de gas maloliente de reacciones de oxidación de xileno mientras al mismo tiempo se reduce el costo de tratamiento de aguas residuales. Más potencia de eje se produce utilizando gas maloliente del que se requiere para impulsar el compresor de aire principal, incluso con temperaturas preferidas de oxidación relativamente baja. De manera simultanea, una cantidad de aguas residuales mayor que el subproducto de agua de la oxidación de xileno se mantiene en forma de vapor y se trata junto con contaminantes de gases malolientes en una unidad de destrucción oxidativa térmica de fase de gas auto-sustentable (auto-aumentable). Opcionalmente, el gas maloliente se combina de múltiples reactores de oxidación de xileno, que comprenden reactores de oxidación primario y/o secundario y formar TPA y/o IPA. Opcionalmente, el condensado del compresor de aire y la purga del depurador acústico se utilizan en un proceso de TPA o como agua de servicio, eliminando efectivamente el flujo normal del efluente líquido de aguas residuales desde una planta de TPA. Opcionalmente, el gas maloliente de PET que contiene el agua de formación de PET se trata en una unidad de destrucción oxidativa térmica compartida, que elimina efectivamente el flujo normal de efluente líquido de aguas residuales desde una planta combinada de pX a TPA a PET.
MX2011004215A 2008-10-31 2009-10-22 Produccion de acido dicarboxilico con destruccion oxidativa auto-alimentable. MX2011004215A (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US11024008P 2008-10-31 2008-10-31
US12/556,099 US9505692B2 (en) 2008-10-31 2009-09-09 Dicarboxylic acid production with self-fuel oxidative destruction
PCT/US2009/005760 WO2010062313A1 (en) 2008-10-31 2009-10-22 Dicarboxylic acid production with self-fuel oxidative destruction

Publications (1)

Publication Number Publication Date
MX2011004215A true MX2011004215A (es) 2012-05-08

Family

ID=42132242

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2011004215A MX2011004215A (es) 2008-10-31 2009-10-22 Produccion de acido dicarboxilico con destruccion oxidativa auto-alimentable.

Country Status (14)

Country Link
US (1) US9505692B2 (es)
EP (1) EP2344440B1 (es)
JP (3) JP2012507516A (es)
KR (1) KR101744360B1 (es)
CN (2) CN102203045A (es)
BR (1) BRPI0920096B1 (es)
CA (1) CA2740833C (es)
ES (1) ES2469799T3 (es)
HK (1) HK1158169A1 (es)
MX (1) MX2011004215A (es)
MY (1) MY156674A (es)
PL (1) PL2344440T3 (es)
PT (1) PT2344440E (es)
WO (1) WO2010062313A1 (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9493387B2 (en) * 2008-10-31 2016-11-15 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with minimal wastewater generation
US9505692B2 (en) 2008-10-31 2016-11-29 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with self-fuel oxidative destruction
US8779208B2 (en) 2012-05-18 2014-07-15 Eastman Chemical Company Process for reducing emissions of volatile organic compounds from the ketonization of carboxylic acids

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3541802A (en) * 1968-06-25 1970-11-24 Judson S Swearingen Recovery of condensable products from gaseous mixtures
JPS62203929A (ja) * 1986-03-04 1987-09-08 Mitsubishi Gas Chem Co Inc 酸化反応器オフガスからの動力化回収方法
US4939297A (en) * 1989-06-05 1990-07-03 Eastman Kodak Company Extraction process for removal of impurities from terephthalic acid filtrate
DE4026732A1 (de) * 1990-08-24 1992-02-27 Huels Chemische Werke Ag Verfahren zur reinigung eines oxidationsabgases mit energierueckgewinnung
US5612007A (en) * 1994-10-14 1997-03-18 Amoco Corporation Apparatus for preparing aromatic carboxylic acids with efficient energy recovery
US5961942A (en) * 1995-06-05 1999-10-05 E. I. Du Pont De Nemours And Company Effluent gas treatment
WO1996039595A1 (en) 1995-06-05 1996-12-12 Imperial Chemical Industries Plc Effluent gas treatment
CA2273958A1 (en) 1996-01-25 1997-07-31 E.I. Du Pont De Nemours And Company Production of aromatic carboxylic acids
US6137001A (en) * 1998-02-11 2000-10-24 Bp Amoco Corporation Process for preparing aromatic carboxylic acids with efficient treatments of gaseous effluent
KR100552262B1 (ko) 1998-05-29 2006-02-20 에치에프엠 인터내쇼날 인코포레이티드 정제된 테레프탈산과 이소프탈산을 혼합 크실렌으로부터제조하는 방법
US7033544B2 (en) * 2000-12-13 2006-04-25 Megtec Systems, Inc. Determination of supplemental fuel requirement and instantaneous control thereof involving regenerative thermal oxidation
US6765070B2 (en) 2001-05-18 2004-07-20 Mitsubishi Chemical Corporation Copolymerized polyester resin composition and stretched film
US6504051B1 (en) 2001-06-04 2003-01-07 Eastman Chemical Company Process for production of aromatic carboxylic acids with improved water removal technique
JP2004257606A (ja) 2003-02-25 2004-09-16 Toray Ind Inc 反応排ガスの処理方法
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
US7351396B2 (en) * 2003-06-05 2008-04-01 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
US7049465B2 (en) * 2003-07-10 2006-05-23 Eastman Chemical Company Process for energy recovery in processes for the preparation of aromatic carboxylic acids
US20060046217A1 (en) * 2004-09-02 2006-03-02 Parker Joseph L Waste treatment system for PTA and PET manufacturing plants
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US20060084017A1 (en) * 2004-10-15 2006-04-20 William Huebner Gas recuperative flameless thermal oxidizer
CN1257146C (zh) 2004-10-19 2006-05-24 浙江大学 对苯二甲酸的生产方法与装置
RU2435754C2 (ru) 2005-03-21 2011-12-10 Бп Корпорейшн Норт Америка Инк. Способ возврата энергии в процессе производства ароматических карбоновых кислот
JP4986105B2 (ja) 2005-09-21 2012-07-25 株式会社吉野工業所 ポリエステル樹脂製の耐熱圧性プラスチックボトル
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7393973B2 (en) * 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
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
US7566802B2 (en) * 2006-05-24 2009-07-28 Eastman Chemical Company Process for energy recovery and water removal in the preparation of aromatic carboxylic acids
US9505692B2 (en) 2008-10-31 2016-11-29 Grupo Petrotemex, S.A. De C.V. Dicarboxylic acid production with self-fuel oxidative destruction

Also Published As

Publication number Publication date
PT2344440E (pt) 2014-06-25
US20100113824A1 (en) 2010-05-06
CA2740833C (en) 2017-11-21
CA2740833A1 (en) 2010-06-03
KR101744360B1 (ko) 2017-06-07
JP2018109040A (ja) 2018-07-12
PL2344440T3 (pl) 2014-09-30
MY156674A (en) 2016-03-15
KR20110091727A (ko) 2011-08-12
EP2344440B1 (en) 2014-04-02
BRPI0920096A2 (pt) 2019-09-17
EP2344440A1 (en) 2011-07-20
CN102203045A (zh) 2011-09-28
BRPI0920096B1 (pt) 2020-10-27
CN106986759A (zh) 2017-07-28
JP2012507516A (ja) 2012-03-29
ES2469799T3 (es) 2014-06-20
JP2015155428A (ja) 2015-08-27
JP7182882B2 (ja) 2022-12-05
RU2011121839A (ru) 2012-12-10
HK1158169A1 (en) 2012-07-13
US9505692B2 (en) 2016-11-29
WO2010062313A1 (en) 2010-06-03

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