KR920016399A - 테레프탈산의 생산방법 - Google Patents

테레프탈산의 생산방법 Download PDF

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Publication number
KR920016399A
KR920016399A KR1019920001597A KR920001597A KR920016399A KR 920016399 A KR920016399 A KR 920016399A KR 1019920001597 A KR1019920001597 A KR 1019920001597A KR 920001597 A KR920001597 A KR 920001597A KR 920016399 A KR920016399 A KR 920016399A
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KR
South Korea
Prior art keywords
mother liquor
precipitate
terephthalic acid
solution
indirectly
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KR1019920001597A
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English (en)
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KR100214397B1 (ko
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힌드마쉬 에릭
아써 터너 존
파커 데이비드
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원본미기재
임페리알 케미칼 인더스트리스 피엘씨
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14Monocyclic dicarboxylic acids
    • C07C63/15Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
    • C07C63/261,4 - Benzenedicarboxylic acid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

내용 없음

Description

테레프탈산의 생산방법.
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명의 공정의 흐름도이다. 제2도는 본 발명의 공정에 사용되는 증류기 컬럼이다.

Claims (8)

  1. 수성 모액을 처리하여 테레프탈산과 제2의 모액으로 이루어진 덜 순순한 침전물을 만든뒤, a) 덜순수한 침전물을 직접 또는 간접적으로 반응 매질로 되돌려 보내는 단계, b)최소한 일부분의 상기 제2모액의 물을 사용하여 직접 또는 처리한 후에 간접적으로 크루드한 고체를 용해시키는 단계; c)상기 제2모액을 분별 증류기를 통과시키거나 또는 리플럭스 시키고 처리된 물을 상기 증류기에서 회수한뒤 환원단계 이후에 나온 용액에서부터 회수한 침전물을 사용하여 세척하는 단계;중 최소한 한 단계를 거치는 것을 특징으로하는 아세트산으로 이루어진 액상 반응 매질내에서 파라크실렌을 산화시켜 테레프탈산을 만들고 이를 액상매질에서부터 크루드한 생성물로 분리해낸다음 물로 이루어진 액체에 용해시켜 용액을 만든뒤 이를 환원조건하에서 불균질한 촉매 및 수소와 접촉시켜 최소한 약간의 불순물들을 제거한뒤 이 용액을 냉각시켜 정제된 고체 침전물 테레프탈산을 침전시키고 이 침전물에서부터 수성 모액을 분리해내는 것으로 구성되는 테레프탈산의 제조방법.
  2. 제1항에 있어서, 단계 a)의 덜순수한 침점물이 수성 모액으로 더 냉각시켜 제조된 방법.
  3. 제2항에 있어서, 수성 모액을 15~100°C의 온도까지 냉각시킨 방법.
  4. 전기항중 어느 한 항에 있어서, 단계 c)의 분별증류가 환류비를 2~10으로 하여 행해진 방법.
  5. 제4항에 있어서, 25~125의 이론단을 사용한 방법.
  6. 제4항 또는 제5항에 있어서, 분별증류하기 위해 되돌려보낸 모액이 컬럼의 탑상으로부터 0-30%의 이론단으로 공급되는 방법.
  7. 전기한 항의 어느 한 항에 있어서, 순수한 테레프탈산을 제조하기위한 침전단계가 최소한 3bar의 압력에서 실시되는 방법.
  8. 전기한 항중 어느 한 항에 있어서, 최소한 일부분의 수성 모액을 사용하여 그 자체로서 직접 또는 처리한 후 간접적으로 크루드 고체를 용해 시키고 및/또는 분별증류기에 통과시킨후 처리된 물을 분별증류기로부터 회수하고 환원 단계후 용액으로부터 회수한 침전물을 세척하는데 사용하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개되는 것임.
KR1019920001597A 1991-02-05 1992-02-01 테레프탈산의 생산방법 KR100214397B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9102393.7 1991-02-05
GB919102393A GB9102393D0 (en) 1991-02-05 1991-02-05 Production of terephthalic acid

Publications (2)

Publication Number Publication Date
KR920016399A true KR920016399A (ko) 1992-09-24
KR100214397B1 KR100214397B1 (ko) 1999-08-02

Family

ID=10689524

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019920001597A KR100214397B1 (ko) 1991-02-05 1992-02-01 테레프탈산의 생산방법

Country Status (12)

Country Link
US (2) US5304676A (ko)
EP (1) EP0498591B2 (ko)
JP (1) JPH0558948A (ko)
KR (1) KR100214397B1 (ko)
CN (2) CN1038580C (ko)
CA (1) CA2059719C (ko)
DE (1) DE69201978T3 (ko)
ES (1) ES2070586T5 (ko)
GB (2) GB9102393D0 (ko)
IN (1) IN185008B (ko)
MX (1) MX9200478A (ko)
TW (1) TW326037B (ko)

Families Citing this family (65)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9104776D0 (en) * 1991-03-07 1991-04-17 Ici Plc Process for the production of terephthalic acid
GB9310070D0 (en) * 1992-05-29 1993-06-30 Ici Plc Process for the production of purified terephthalic acid
GB9303191D0 (en) * 1993-02-17 1993-03-31 Ici Plc Separation process
EG20284A (en) * 1993-02-17 1998-07-30 Ici Plc Separation process
US5612007A (en) * 1994-10-14 1997-03-18 Amoco Corporation Apparatus for preparing aromatic carboxylic acids with efficient energy recovery
CN1163693C (zh) * 1995-06-05 2004-08-25 纳幕尔杜邦公司 废气处理方法
US5961942A (en) * 1995-06-05 1999-10-05 E. I. Du Pont De Nemours And Company Effluent gas treatment
US5929274A (en) 1995-06-07 1999-07-27 Hfm International, Inc. Method to reduce carboxybenzaldehyde isomers in terephthalic acid or isophthalic acid
US5767311A (en) 1995-06-07 1998-06-16 Glitsch International, Inc. Method and apparatus for preparing purified terephtalic acid
US6013835A (en) 1995-06-07 2000-01-11 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid
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
WO1997024311A1 (en) * 1995-12-30 1997-07-10 Sunkyong Industries Co., Ltd. Process for manufacturing terephthalic acid
TR199902222T2 (xx) * 1997-03-14 2000-02-21 E.I. Du Pont De Nemours & Company Organik asit içeren akışkan akımların tedavisi.
GB9705349D0 (en) 1997-03-14 1997-04-30 Ici Plc Treatment of effluent streams
US6137001A (en) * 1998-02-11 2000-10-24 Bp Amoco Corporation Process for preparing aromatic carboxylic acids with efficient treatments of gaseous effluent
US6765113B2 (en) 2000-07-19 2004-07-20 E.I. Du Pont De Nemours And Company Production of aromatic carboxylic acids
DE60141420D1 (de) * 2001-05-15 2010-04-08 Mitsubishi Chem Corp Verfahren zur herstellung einer verbindung
US7485747B2 (en) * 2001-06-04 2009-02-03 Eastman Chemical Company Two stage oxidation process for the production of aromatic dicarboxylic acids
US7196215B2 (en) * 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
ITMI20021423A1 (it) * 2002-06-27 2003-12-29 Eurotecnica Dev & Licensing S Processo per la separazione dell'acqua prodotta nella ossidazione catalitica di idrocarburi aromatici ad acidi aromatici policarbossilici
KR20050025318A (ko) * 2002-07-09 2005-03-14 인비스타 테크놀러지스 에스.에이.알.엘 초임계 조건하의 방향족 디카르복실산의 제조 방법
CN1982283A (zh) * 2003-01-07 2007-06-20 三菱化学株式会社 制备高纯度对苯二甲酸的方法
AU2003292740A1 (en) * 2003-01-10 2004-08-10 Mitsubishi Chemical Corporation Process for producing aromatic carboxylic acid and process for producing terephthalic acid
US20050256335A1 (en) * 2004-05-12 2005-11-17 Ovidiu Marin Providing gases to aromatic carboxylic acid manufacturing processes
WO2005115957A1 (ja) * 2004-05-28 2005-12-08 Mitsubishi Chemical Corporation 高純度テレフタル酸の製造方法
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7615663B2 (en) * 2004-09-02 2009-11-10 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) * 2004-11-29 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
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 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
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
UA96569C2 (ru) * 2005-03-21 2011-11-25 Бипи Корпорейшн Норт Америка Инк. Процесс и устройство для изготовления ароматических карбоновых кислот
US20090018361A1 (en) * 2005-03-22 2009-01-15 Mitsubishi Chemical Corporation Process of producing high purity terephthalic acid
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
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
CN100368370C (zh) * 2006-03-29 2008-02-13 中国石化仪征化纤股份有限公司 对二甲苯氧化母液中悬浮物的回收系统装置
CN101152969B (zh) * 2006-09-29 2011-01-19 中国石油化工股份有限公司石油化工科学研究院 对苯二甲酸生产废水的处理方法
CN102026952B (zh) * 2008-05-20 2014-05-07 株式会社日立制作所 精制对苯二甲酸分离母液的处理方法
BRPI1006621A2 (pt) 2009-04-24 2016-04-19 INVISTA Technologies S à r l "método de resfriar uma corrente de água-mãe"
UA112991C2 (uk) 2011-08-16 2016-11-25 Пурак Біокем Б.В. Відновлення карбонової кислоти з магнієвих солей шляхом осаджування з використанням хлористоводневої кислоти для створення ферментивного поживного середовища
AU2012295627B2 (en) * 2011-08-16 2016-05-12 Purac Biochem B.V. Recovery of carboxylic acid from their magnesium salts by precipitation using hydrochloric acid, useful for fermentation broth work-up
CN102798679B (zh) * 2012-09-03 2014-01-15 绍兴汉青环保科技有限公司 一种pta 生产装置气体中有机物的气相色谱分析方法
US9428436B2 (en) 2013-12-18 2016-08-30 Bp Corporation North America Inc. Process and apparatus for manufacturing aromatic carboxylic acids
WO2017081610A1 (en) 2015-11-13 2017-05-18 Sabic Global Technologies B.V. Process using ion exchange resins for the treatment of wastewater emanating from purified terephthalic acid production
CN113318471A (zh) * 2021-07-08 2021-08-31 山东友道化学有限公司 二甲苯氧化反应液的处理方法及系统

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2849483A (en) * 1954-07-30 1958-08-26 Chemstrand Corp Method of purifying aromatic dicarboxylic acids
GB970492A (en) * 1960-10-18 1964-09-23 Standard Oil Co Production of aromatic carboxylic acids
GB970491A (en) * 1960-10-18 1964-09-23 Standard Oil Co Production of aromatic carboxylic acids
NL6606774A (ko) * 1965-05-17 1966-11-18
FR1569704A (ko) * 1968-02-26 1969-06-06
US3592847A (en) * 1968-05-02 1971-07-13 Allied Chem Process for the purification of terephthalic acid
GB1373230A (en) * 1971-12-23 1974-11-06 Mitsui Petrochemical Ind Process for producing terephthalic acid
JPS52128344A (en) * 1976-04-20 1977-10-27 Mitsubishi Gas Chem Co Inc Preparation of high-purity terephthalic acid
US4467111A (en) * 1981-10-29 1984-08-21 Standard Oil Company (Indiana) Process for purification of crude terephthalic acid
US5166420A (en) * 1986-10-20 1992-11-24 Mitsui Petrochemical Industries, Ltd. Process for the production of high purity terephthalic acid
US4933492A (en) * 1988-10-13 1990-06-12 Amoco Corporation Purification of crude isophthalic acid

Also Published As

Publication number Publication date
CN1130328C (zh) 2003-12-10
EP0498591A2 (en) 1992-08-12
EP0498591B2 (en) 2004-10-13
GB9202241D0 (en) 1992-03-18
US5304676A (en) 1994-04-19
JPH0558948A (ja) 1993-03-09
CN1038580C (zh) 1998-06-03
EP0498591B1 (en) 1995-04-12
CA2059719C (en) 2002-10-08
USRE36008E (en) 1998-12-22
MX9200478A (es) 1992-08-01
KR100214397B1 (ko) 1999-08-02
DE69201978D1 (de) 1995-05-18
ES2070586T3 (es) 1995-06-01
CA2059719A1 (en) 1992-08-06
DE69201978T3 (de) 2005-03-10
CN1064675A (zh) 1992-09-23
DE69201978T2 (de) 1995-08-24
TW326037B (en) 1998-02-01
CN1150944A (zh) 1997-06-04
ES2070586T5 (es) 2005-05-01
IN185008B (ko) 2000-10-21
GB9102393D0 (en) 1991-03-20
EP0498591A3 (en) 1993-01-27

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