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BRPI0401876A - Processo para recuperação de catalisador de metal de um licor mãe, corrente de impurezas orgânicas com alto ponto de ebulição, corrente rica em solvente, processo para produção de uma corrente de licor mãe superconcentrado, e, composição - Google Patents

Processo para recuperação de catalisador de metal de um licor mãe, corrente de impurezas orgânicas com alto ponto de ebulição, corrente rica em solvente, processo para produção de uma corrente de licor mãe superconcentrado, e, composição

Info

Publication number
BRPI0401876A
BRPI0401876A BR0401876-1A BRPI0401876A BRPI0401876A BR PI0401876 A BRPI0401876 A BR PI0401876A BR PI0401876 A BRPI0401876 A BR PI0401876A BR PI0401876 A BRPI0401876 A BR PI0401876A
Authority
BR
Brazil
Prior art keywords
stream
mother liquor
superconcentrated
metal catalyst
solvent
Prior art date
Application number
BR0401876-1A
Other languages
English (en)
Inventor
Robert Lin
Marcel De Vreede
Original Assignee
Eastman Chem 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 Eastman Chem Co filed Critical Eastman Chem Co
Publication of BRPI0401876A publication Critical patent/BRPI0401876A/pt

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
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/06—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using steam
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/48—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
    • 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)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

"PROCESSO PARA RECUPERAçãO DE CATALISADOR DE METAL DE UM LICOR MãE, CORRENTE DE IMPUREZAS ORGâNICAS COM ALTO PONTO DE EBULIçãO, CORRENTE RICA EM SOLVENTE, PROCESSO PARA PRODUçãO DE UMA CORRENTE DE LICOR MãE SUPERCONCENTRADO, E, COMPOSIçãO". Método para remoção de impurezas de um licor mãe que compreende um ácido carboxílico, um catalisador de metal e impurezas por (a) evaporar o licor mãe que compreende ácido carboxílico, um catalisador de metal, impurezas e um solvente em uma primeira zona de evaporador para produzir uma corrente de vapor e uma corrente de licor mãe concentrado; (b) evaporar a corrente de licor mãe concentrado em uma segunda zona de evaporador para formar uma corrente rica em solvente e uma corrente de licor mãe superconcentrado; (c) misturar em uma zona de mistura uma solução água-solvente e opcionalmente um solvente de extração com a corrente de licor mãe superconcentrado para formar uma mistura aquosa; (d) opcionalmente separar as impurezas orgânicas da mistura aquosa em uma zona de separação sólido-líquido para formar uma mistura aquosa purificada; e (e) extrair a mistura aquosa ou a mistura aquosa purificada com um solvente de extração em uma zona de extração para formar uma corrente de extrato e uma corrente de rafinado.
BR0401876-1A 2003-06-05 2004-05-31 Processo para recuperação de catalisador de metal de um licor mãe, corrente de impurezas orgânicas com alto ponto de ebulição, corrente rica em solvente, processo para produção de uma corrente de licor mãe superconcentrado, e, composição BRPI0401876A (pt)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/455,018 US7381386B2 (en) 2003-06-05 2003-06-05 Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid

Publications (1)

Publication Number Publication Date
BRPI0401876A true BRPI0401876A (pt) 2005-01-04

Family

ID=33159563

Family Applications (1)

Application Number Title Priority Date Filing Date
BR0401876-1A BRPI0401876A (pt) 2003-06-05 2004-05-31 Processo para recuperação de catalisador de metal de um licor mãe, corrente de impurezas orgânicas com alto ponto de ebulição, corrente rica em solvente, processo para produção de uma corrente de licor mãe superconcentrado, e, composição

Country Status (12)

Country Link
US (1) US7381386B2 (pt)
EP (1) EP1484306A1 (pt)
JP (1) JP2004358465A (pt)
KR (1) KR101169469B1 (pt)
CN (1) CN1572767B (pt)
AR (1) AR044617A1 (pt)
BR (1) BRPI0401876A (pt)
CA (1) CA2467001C (pt)
MX (1) MXPA04005330A (pt)
MY (1) MY141870A (pt)
RU (1) RU2347773C2 (pt)
TW (1) TW200505846A (pt)

Families Citing this family (68)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7282151B2 (en) * 2003-06-05 2007-10-16 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7351396B2 (en) 2003-06-05 2008-04-01 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
US7410632B2 (en) * 2003-06-05 2008-08-12 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US7452522B2 (en) * 2003-06-05 2008-11-18 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
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
US7381386B2 (en) 2003-06-05 2008-06-03 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US7888530B2 (en) * 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7897810B2 (en) 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company 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
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US20070238899A9 (en) * 2004-09-02 2007-10-11 Robert Lin Optimized production of aromatic dicarboxylic acids
US7381836B2 (en) 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 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
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7291270B2 (en) 2004-10-28 2007-11-06 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7273559B2 (en) 2004-10-28 2007-09-25 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7884231B2 (en) * 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
US7919652B2 (en) * 2005-05-19 2011-04-05 Eastman Chemical Company Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone
US20060264662A1 (en) * 2005-05-19 2006-11-23 Gibson Philip E Esterification of an enriched composition
US7557243B2 (en) 2005-05-19 2009-07-07 Eastman Chemical Company Enriched terephthalic acid composition
US7304178B2 (en) 2005-05-19 2007-12-04 Eastman Chemical Company Enriched isophthalic acid composition
US7432395B2 (en) 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
US7741516B2 (en) * 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US7834208B2 (en) * 2005-05-19 2010-11-16 Eastman Chemical Company Process to produce a post catalyst removal composition
US20060264664A1 (en) * 2005-05-19 2006-11-23 Parker Kenny R Esterification of an exchange solvent enriched composition
US7880031B2 (en) * 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
US20060264656A1 (en) * 2005-05-19 2006-11-23 Fujitsu Limited Enrichment process using compounds useful in a polyester process
US7897809B2 (en) * 2005-05-19 2011-03-01 Eastman Chemical Company Process to produce an enrichment feed
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7402694B2 (en) * 2005-08-11 2008-07-22 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7569722B2 (en) * 2005-08-11 2009-08-04 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
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
US7880032B2 (en) * 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7462736B2 (en) * 2006-03-01 2008-12-09 Eastman Chemical Company Methods and apparatus for isolating carboxylic acid
US7863481B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US7847121B2 (en) * 2006-03-01 2010-12-07 Eastman Chemical Company Carboxylic acid production process
US20070203359A1 (en) * 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US7888529B2 (en) * 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US20070208199A1 (en) * 2006-03-01 2007-09-06 Kenny Randolph Parker Methods and apparatus for isolating carboxylic acid
US8697906B2 (en) * 2006-03-01 2014-04-15 Grupo Petrotemex, S.A. De C.V. Methods and apparatus for producing a low-moisture carboxylic acid wet cake
US8173836B2 (en) * 2006-03-01 2012-05-08 Grupo Petrotemex, S.A. De C.V. Method and apparatus for drying carboxylic acid
US7863483B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Carboxylic acid production process
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
BR112012029158A2 (pt) 2010-05-18 2016-09-13 Invista Tech Sarl processo de fabricação de ácido policarboxílico aromático e de ácido tereftálico
US8382961B2 (en) * 2010-06-07 2013-02-26 Amt International, Inc. System and method for reduction of water consumption in purified terephthalic acid production
US8167974B2 (en) * 2010-08-20 2012-05-01 Grupo Petrotemex, S.A. De C.V. Terephthalic acid purge filtration rate by controlling % water in filter feed slurry
US9963413B2 (en) * 2010-08-20 2018-05-08 Grupo Petrotemex, S.A. De C.V. Terephthalic acid purge filtration rate by controlling % water in filter feed slurry
DE102013000027A1 (de) * 2013-01-03 2014-07-03 Thyssenkrupp Industrial Solutions Ag Verfahren zur Aufreinigung von Carbonsäuren aus Fermentationsbrühen
CN105668677A (zh) * 2014-11-17 2016-06-15 河南龙成煤高效技术应用有限公司 一种煤化工废水油酚协同萃取剂

Family Cites Families (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2964559A (en) * 1957-11-12 1960-12-13 Standard Oil Co Process for recovery of oxidation catalysts
GB892766A (en) 1957-11-12 1962-03-28 Standard Oil Co Improvements in or relating to the production of aromatic acids
US3673154A (en) 1970-06-26 1972-06-27 Atlantic Richfield Co Process for the recovery of cobalt catalyst
US3873468A (en) * 1970-12-09 1975-03-25 Kuraray Yuka Kk Method of removing substance harmful to oxidation reaction in the production of benzenecarboxylic acids by oxidation
JPS4914637B1 (pt) * 1970-12-09 1974-04-09
JPS4914636B1 (pt) * 1970-12-09 1974-04-09
BE792519A (fr) 1971-12-10 1973-06-08 Standard Oil Co Recuperation de metaux catalytiques des residus de la production d'acides aromatiques par oxydation catalytique en phase liquide
US3840641A (en) * 1972-10-20 1974-10-08 Standard Oil Co Recovery of bromine from tere-and isophthalic acid process residues
JPS557302B2 (pt) 1973-03-30 1980-02-23
JPS5328420B2 (pt) * 1973-04-05 1978-08-15
JPS5328421B2 (pt) * 1973-05-15 1978-08-15
JPS51145488A (en) 1976-05-31 1976-12-14 Wako Pure Chem Ind Ltd Reclaiming method of catalyst for liquid phase oxidation
US4185073A (en) * 1976-07-26 1980-01-22 Standard Oil Company (Indiana) Apparatus for iso- or terephthalic acid production in and recovery from benzoic acid-water solvent system
US4081464A (en) * 1976-07-26 1978-03-28 Standard Oil Company Iso- or terephthalic acid production in and recovery from benzoic acid-water solvent system
NL188282C (nl) * 1977-04-04 1992-05-18 Montedison Spa Werkwijze voor de synthese van tereftaalzuur door oxyderen van p-xyleen in azijnzuuroplossing.
US4158738A (en) * 1977-05-26 1979-06-19 E. I. Du Pont De Nemours And Company Process for the production of fiber-grade terephthalic acid
US4330676A (en) * 1977-07-04 1982-05-18 Imperial Chemical Industries Limited Oxidation process
JPS5425292A (en) 1977-07-28 1979-02-26 Mitsubishi Chem Ind Ltd Method of recovering liquid phase oxidation catalyst of terephthalic acid
US4219669A (en) * 1979-06-08 1980-08-26 Jgc Corporation Method of treating mother liquor of reaction in terephthalic acid production
SU1091851A3 (ru) * 1979-07-02 1984-05-07 Джей Джи Си Корпорейшн (Фирма) Способ обработки реакционного маточного раствора при производстве терефталевой кислоты
IT1129759B (it) * 1980-01-23 1986-06-11 Montedison Spa Metodo per ricuperare in forma attiva i componenti del sistema catalitico della sintesi dell'acido tereftalico
US4298580A (en) * 1980-12-19 1981-11-03 Standard Oil Company (Indiana) Separation of cobalt and manganese from trimellitic acid process residue by precipitating as carbonates, redissolving as halides and removing cobalt by magnetic means
JPS58174344A (ja) 1982-04-05 1983-10-13 Kuraray Yuka Kk 酢酸の回収方法
JPS5953441A (ja) 1982-09-20 1984-03-28 Mitsubishi Chem Ind Ltd 芳香族カルボン酸の製造法
GB8428028D0 (en) * 1984-11-06 1984-12-12 Ici Plc Recovery of metal catalyst residues
US4769489A (en) * 1986-07-28 1988-09-06 Amoco Corporation Catalyst recovery method
US4914230A (en) * 1986-07-28 1990-04-03 Amoco Corporation Catalyst recovery method
KR910005989B1 (ko) 1988-11-30 1991-08-09 삼성석유화학 주식회사 테레프탈산 제조공정의 용매 정제법
US4939297A (en) 1989-06-05 1990-07-03 Eastman Kodak Company Extraction process for removal of impurities from terephthalic acid filtrate
JP2924104B2 (ja) * 1990-06-25 1999-07-26 三菱瓦斯化学株式会社 高純度イソフタル酸の製造方法
SG80548A1 (en) 1991-04-12 2001-05-22 Amoco Corp Process for preparation of terephthalic acid
US5200557A (en) * 1991-04-12 1993-04-06 Amoco Corporation Process for preparation of crude terephthalic acid suitable for reduction to prepare purified terephthalic acid
US5175355A (en) 1991-04-12 1992-12-29 Amoco Corporation Improved process for recovery of purified terephthalic acid
GB9211415D0 (en) 1992-05-29 1992-07-15 Ici Plc Process for the production of purified terephthalic acid
JP3232678B2 (ja) 1992-08-18 2001-11-26 住友化学工業株式会社 酢酸の回収方法
JP3211396B2 (ja) 1992-08-26 2001-09-25 住友化学工業株式会社 アクリル酸及び酢酸の回収方法
GB9302333D0 (en) * 1993-02-05 1993-03-24 Ici Plc Filtration process
JPH06327915A (ja) * 1993-05-24 1994-11-29 Mitsui Petrochem Ind Ltd スラリーから結晶を回収する方法及び装置
JP3332594B2 (ja) * 1994-08-12 2002-10-07 ダイセル化学工業株式会社 酢酸の精製方法
US6054610A (en) * 1995-06-07 2000-04-25 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid and isophthalic acid from mixed xylenes
JP3202150B2 (ja) 1995-08-04 2001-08-27 昭和電工株式会社 酢酸の精製方法
JP3729284B2 (ja) * 1995-09-22 2005-12-21 三菱瓦斯化学株式会社 高純度テレフタル酸の製造方法
JPH09157214A (ja) 1995-10-05 1997-06-17 Mitsubishi Chem Corp 芳香族カルボン酸の製造方法
EP0879221A1 (en) 1996-01-25 1998-11-25 E.I. Du Pont De Nemours And Company Production of aromatic carboxylic acids
KR100463612B1 (ko) 1996-02-22 2005-02-28 이.아이,듀우판드네모아앤드캄파니 방향족폴리카르복실산의제조방법
US5840965A (en) * 1996-06-24 1998-11-24 E. I. Du Pont De Nemours And Company Process for the production of purified telephthalic acid
JP3757995B2 (ja) * 1996-07-12 2006-03-22 三菱瓦斯化学株式会社 高純度イソフタル酸の製造方法
US5955394A (en) * 1996-08-16 1999-09-21 Mobile Process Technology, Co. Recovery process for oxidation catalyst in the manufacture of aromatic carboxylic acids
JPH10114699A (ja) 1996-10-07 1998-05-06 Teijin Ltd 酢酸の回収方法
US5988394A (en) * 1996-11-28 1999-11-23 Kabushiki Kaisha Toshiba Tray for containing parts for storage and transportation
JPH11165079A (ja) * 1997-12-05 1999-06-22 Toray Ind Inc 液相空気酸化反応における酢酸回収方法および触媒回収方法
JPH11349529A (ja) 1998-06-05 1999-12-21 Mitsui Chem Inc 芳香族カルボン酸の製造方法
CN1264798C (zh) * 1998-11-24 2006-07-19 文森特·T·D·林 高纯度芳香多羧酸及其衍生物的纯化及制造方法
US6153790A (en) * 1998-12-01 2000-11-28 Shell Oil Company Method to produce aromatic dicarboxylic acids using cobalt and zirconium catalysts
CN1424996A (zh) 2000-01-25 2003-06-18 因卡国际公司 天然对苯二酸(“cta”)的回收方法
JP4788023B2 (ja) * 2000-06-27 2011-10-05 三菱瓦斯化学株式会社 液相酸化反応母液からの触媒成分の回収方法
US7196215B2 (en) * 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
US7132566B2 (en) * 2003-09-22 2006-11-07 Eastman Chemical Company Process for the purification of a crude carboxylic acid slurry
US7074954B2 (en) * 2002-12-09 2006-07-11 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
US7381386B2 (en) 2003-06-05 2008-06-03 Eastman Chemical Company Extraction process for removal of impurities from mother liquor 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
US7282151B2 (en) * 2003-06-05 2007-10-16 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7410632B2 (en) * 2003-06-05 2008-08-12 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid

Also Published As

Publication number Publication date
CA2467001A1 (en) 2004-12-05
CN1572767B (zh) 2013-03-13
CN1572767A (zh) 2005-02-02
KR20040108588A (ko) 2004-12-24
KR101169469B1 (ko) 2012-07-30
AR044617A1 (es) 2005-09-21
RU2347773C2 (ru) 2009-02-27
EP1484306A1 (en) 2004-12-08
MXPA04005330A (es) 2004-12-08
JP2004358465A (ja) 2004-12-24
CA2467001C (en) 2009-10-20
RU2004117064A (ru) 2006-01-10
US7381386B2 (en) 2008-06-03
MY141870A (en) 2010-07-16
US20040249208A1 (en) 2004-12-09
TW200505846A (en) 2005-02-16

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