JP2001521917A5 - - Google Patents

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Publication number
JP2001521917A5
JP2001521917A5 JP2000518932A JP2000518932A JP2001521917A5 JP 2001521917 A5 JP2001521917 A5 JP 2001521917A5 JP 2000518932 A JP2000518932 A JP 2000518932A JP 2000518932 A JP2000518932 A JP 2000518932A JP 2001521917 A5 JP2001521917 A5 JP 2001521917A5
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JP
Japan
Prior art keywords
terephthalic acid
solution
purified terephthalic
temperature
stage
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.)
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Application number
JP2000518932A
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English (en)
Japanese (ja)
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JP4381600B2 (ja
JP2001521917A (ja
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Publication date
Priority claimed from US08/962,030 external-priority patent/US5840968A/en
Application filed filed Critical
Publication of JP2001521917A publication Critical patent/JP2001521917A/ja
Publication of JP2001521917A5 publication Critical patent/JP2001521917A5/ja
Application granted granted Critical
Publication of JP4381600B2 publication Critical patent/JP4381600B2/ja
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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JP2000518932A 1997-10-31 1998-10-29 精製テレフタル酸を製造する方法及び装置 Expired - Fee Related JP4381600B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US08/962,030 US5840968A (en) 1995-06-07 1997-10-31 Method and apparatus for preparing purified terephthalic acid
US08/962,030 1997-10-31
PCT/US1998/022942 WO1999023055A1 (en) 1997-10-31 1998-10-29 Method and apparatus for preparing purified terephthalic acid

Publications (3)

Publication Number Publication Date
JP2001521917A JP2001521917A (ja) 2001-11-13
JP2001521917A5 true JP2001521917A5 (enExample) 2006-01-05
JP4381600B2 JP4381600B2 (ja) 2009-12-09

Family

ID=25505339

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000518932A Expired - Fee Related JP4381600B2 (ja) 1997-10-31 1998-10-29 精製テレフタル酸を製造する方法及び装置

Country Status (17)

Country Link
US (1) US5840968A (enExample)
EP (1) EP1030829B1 (enExample)
JP (1) JP4381600B2 (enExample)
KR (1) KR100603723B1 (enExample)
CN (1) CN1127471C (enExample)
AR (1) AR017765A1 (enExample)
AU (1) AU1286899A (enExample)
BR (1) BR9813349B1 (enExample)
CA (1) CA2307783C (enExample)
DE (1) DE69835229T2 (enExample)
ES (1) ES2263227T3 (enExample)
ID (1) ID21201A (enExample)
MY (1) MY119529A (enExample)
RU (1) RU2213725C2 (enExample)
TR (1) TR200001138T2 (enExample)
TW (1) TW505627B (enExample)
WO (1) WO1999023055A1 (enExample)

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KR100642625B1 (ko) * 1998-11-24 2006-11-10 티. 디. 빈센트 린 고순도 방향족 폴리카르복실산 및 이것의 유도체를 정제및 생성하는 방법
US6392091B2 (en) * 1998-11-24 2002-05-21 Tsong-Dar Vincent Lin Process of purifying and producing high purity aromatic polycarboxylic acids
KR20020048395A (ko) 1999-08-30 2002-06-22 모씨 앤드 기솔피 오버시즈 소시에떼아노님 2,6-나프탈렌 디카르복실산의 제조를 위한 종합 방법
US6649263B2 (en) 2001-11-16 2003-11-18 Honeywell International Inc. Polyester resin and industrial yarn process
DE10206168A1 (de) * 2002-02-14 2003-08-21 Guehring Joerg Kupplung für mudular aufgebaute Werkzeughalterarme
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US7161027B2 (en) 2002-12-09 2007-01-09 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
CN100453517C (zh) * 2003-01-10 2009-01-21 三菱化学株式会社 芳香羧酸的制备方法和对苯二甲酸的制备方法
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US20050059709A1 (en) * 2003-09-15 2005-03-17 Meythaler Jay M. Treatment of a neuropathy with rapid release aminopyridine
US7214760B2 (en) * 2004-01-15 2007-05-08 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
RU2395486C2 (ru) * 2004-04-09 2010-07-27 ДжиТиСи ТЕКНОЛОДЖИ ИНК. Очистка карбоновых кислот путем комплексообразования с селективными растворителями
US20050288527A1 (en) * 2004-06-28 2005-12-29 Cook William L Method for preparing free-flowing crystalline material
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) 2004-09-02 2009-03-24 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
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) 2004-09-02 2009-08-04 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
US7910769B2 (en) 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
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
US7880031B2 (en) * 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
US7432395B2 (en) * 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
US7557243B2 (en) 2005-05-19 2009-07-07 Eastman Chemical Company Enriched terephthalic acid composition
US7834208B2 (en) * 2005-05-19 2010-11-16 Eastman Chemical Company Process to produce a post catalyst removal composition
US7304178B2 (en) * 2005-05-19 2007-12-04 Eastman Chemical Company Enriched isophthalic acid composition
US7741516B2 (en) 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US20060264662A1 (en) * 2005-05-19 2006-11-23 Gibson Philip E Esterification of an enriched composition
US20060264664A1 (en) * 2005-05-19 2006-11-23 Parker Kenny R Esterification of an exchange solvent enriched composition
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
US7884231B2 (en) * 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
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
US20070179312A1 (en) * 2006-02-02 2007-08-02 O'meadhra Ruairi Seosamh Process for the purification of a crude carboxylic axid slurry
US8173835B2 (en) * 2006-03-01 2012-05-08 Grupo Petrotemex, S.A. De C.V. Method and apparatus for drying 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
US7888529B2 (en) 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US8614350B2 (en) 2008-01-15 2013-12-24 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8455680B2 (en) 2008-01-15 2013-06-04 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
MX2011011148A (es) 2009-04-24 2012-01-27 Invista Tech Sarl Metodos, procesos y sistemas para el tratamiento y purificacion de acido tereftalico crudo y corrientes de proceso asociadas.
CN103069554A (zh) * 2010-08-23 2013-04-24 索尼公司 有机薄膜的形成方法、有机薄膜的形成装置以及有机器件的制造方法
CN102234226A (zh) * 2010-09-02 2011-11-09 华东理工大学 一种从碱减量废液中回收提纯对苯二甲酸的方法
CN102179063A (zh) * 2011-03-23 2011-09-14 苏州汇通色谱分离纯化有限公司 高压液-液萃取方法
CN103030554B (zh) * 2011-09-30 2015-04-08 中国石油化工股份有限公司 溶剂置换粗对苯二甲酸氧化浆料的方法
CN103121943B (zh) * 2011-11-18 2015-08-12 中国石油化工股份有限公司 提纯粗间苯二甲酸氧化浆料的方法
RU2475475C1 (ru) * 2011-12-26 2013-02-20 Открытое акционерное общество "Каустик" (ОАО "Каустик") Способ получения диамида терефталевой кислоты
US8927764B2 (en) 2011-12-29 2015-01-06 Uop Llc Process for producing terephthalic acid
US8697905B2 (en) 2011-12-29 2014-04-15 Uop Llc Process for producing terephthalic acid
US9024059B2 (en) 2011-12-29 2015-05-05 Uop Llc Process for producing terephthalic acid
US9156765B2 (en) 2011-12-29 2015-10-13 Uop Llc Process for oxidizing alkyl-aromatic compounds
US8759571B2 (en) 2011-12-29 2014-06-24 Uop Llc Process for oxidizing alkyl-aromatic compounds
US9045408B2 (en) 2011-12-29 2015-06-02 Uop Llc Process for oxidizing alkyl-aromatic compounds
US9085522B2 (en) 2011-12-29 2015-07-21 Uop Llc Process for producing terephthalic acid
US9150484B2 (en) 2011-12-29 2015-10-06 Uop Llc Process for producing terephthalic acid
CN108623065B (zh) * 2017-03-22 2020-08-25 天华化工机械及自动化研究设计院有限公司 Pta精制单元母液的回收利用方法
EP4341335A1 (en) 2021-05-20 2024-03-27 Carbios Process for degrading a plastic product comprising at least one polyester
JP2024519032A (ja) 2021-05-20 2024-05-08 キャルビオス 少なくとも１種のポリエステルを含むプラスチック製品を分解するための方法
WO2023003277A1 (ko) * 2021-07-19 2023-01-26 주식회사 엘지화학 재활용 플라스틱 합성용 단량체 조성물, 이의 제조방법, 그리고 이를 이용한 재활용 플라스틱, 성형품 및 가소제 조성물
CN118369423A (zh) 2021-11-16 2024-07-19 卡比奥斯公司 酯酶的用途
CN120864981A (zh) * 2025-09-22 2025-10-31 浙江工业大学 一种印染白泥绿色资源化利用的工艺

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