KR850001723A - p-크실렌으로부터 테레프탈산의 제조방법 - Google Patents

p-크실렌으로부터 테레프탈산의 제조방법 Download PDF

Info

Publication number
KR850001723A
KR850001723A KR1019840004665A KR840004665A KR850001723A KR 850001723 A KR850001723 A KR 850001723A KR 1019840004665 A KR1019840004665 A KR 1019840004665A KR 840004665 A KR840004665 A KR 840004665A KR 850001723 A KR850001723 A KR 850001723A
Authority
KR
South Korea
Prior art keywords
gas
xylene
terephthalic acid
reaction
adjusted
Prior art date
Application number
KR1019840004665A
Other languages
English (en)
Other versions
KR910006326B1 (ko
Inventor
히로시(외 1) 하시즈메
Original Assignee
스즈끼 샤부로오
미쓰비시 가가꾸 고오교오 가부시끼 가이샤
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 스즈끼 샤부로오, 미쓰비시 가가꾸 고오교오 가부시끼 가이샤 filed Critical 스즈끼 샤부로오
Publication of KR850001723A publication Critical patent/KR850001723A/ko
Application granted granted Critical
Publication of KR910006326B1 publication Critical patent/KR910006326B1/ko

Links

Classifications

    • 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
    • C07C51/16Preparation 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
    • 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

p-크실렌으로부터 테레프탈산의 제조방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 p-크실렌의 주산화를 위한 반응용기의 개략도해이다.

Claims (9)

  1. p-크실렌을 산화하기 위하여 사용되는 반응용기로부터의 배기가스내에 포함된 산소가스의 농도가 2내지 8부피%인 아세트산 용매내에서 180내지 230℃의 온도에서 코발트, 망간 및 브롬을 포함하는 촉매의 존재하에 공기에 의하여 p-크실렌을 테레프탈산으로 산화시키는, p-크실렌으로부터 테레프탈산을 연속제조하는 방법에 있어서,
    (a) 상기 반응용기로부터 끌어낸 기체를 이 기체로 부터 응축물을 제거하기 위하여 응축시켜 이로써 산화배기가스를 제조하는 단계와, (b) 재순환가스의 방출가스에 대한 부피비가 0.3내지 5이고 상기 방출가스는 반응계의 외부로 배기되도록 하는, 제조된 산화배기가스를 방출가스와 재순환가스로 분할하는 단계, (c) 상기 재순환가스를 상기 반응용기의 액상에 계속적으로 공급하는 단계, 그리고 (d) 상기 재순환가 스가공급되지 않는 반응상태보다 더 높은 반응압력하에 p-크실렌의 산화반응을 수행하는 단계, 들로 이루어지는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산을 연속적으로 제조하는 방법.
  2. 제1항에 있어서, 반응용기의 기체상내의 응축가스에 대한 비응축가스의 압력비는 0.65내지 3으로 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산을 제조하는 방법.
  3. 제1항에 있어서, 재순환가스의 공급량은 반응기의 기체상내의 산소가스의 부분압이 상기 재순환가스가 공급되지 않는 반응조건보다 1.3내지 5배 높도록 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  4. 제1항 내지 제3항중의 어느하나에 있어서, p-크실렌의 산화를 위한 반응계의 수분농도는 7내지 14중량%로 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  5. 제1항 내지 제3항중 어느하나에 있어서, 산화반응은 180℃내지 22℃의 온도에서 수행되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  6. 제1항 내지 제3항중 어느하나에 있어서, 산화배기가스중의 산소의 농도가 4내지 7중량%로 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  7. 제1항 내지 제3항중 어느하나에 있어서, 방출가스에 대한 재순환가스의 부피비는 0.5내지 3으로 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  8. 제2항에 있어서, 응축가스에 대한 비응축가스의 압력비는 0.7내지 2로 조정되는 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
  9. 제3항에 있어서, 반응기의 기체상의 산소가스의 부분압은 재순환가스가 공급되지 않는 반응조건보다 1.5내지 3배 높은 것을 특징으로 하는 p-크실렌으로부터 테레프탈산의 제조방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019840004665A 1983-08-09 1984-08-04 p-크실렌으로부터 테레프탈산의 제조방법 KR910006326B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP83-145407 1983-08-09
JP58145407A JPS6036439A (ja) 1983-08-09 1983-08-09 テレフタル酸の製法
JP58-145407 1983-08-09

Publications (2)

Publication Number Publication Date
KR850001723A true KR850001723A (ko) 1985-04-01
KR910006326B1 KR910006326B1 (ko) 1991-08-20

Family

ID=15384538

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019840004665A KR910006326B1 (ko) 1983-08-09 1984-08-04 p-크실렌으로부터 테레프탈산의 제조방법

Country Status (5)

Country Link
US (1) US4593122A (ko)
EP (1) EP0135341B1 (ko)
JP (1) JPS6036439A (ko)
KR (1) KR910006326B1 (ko)
DE (1) DE3466978D1 (ko)

Families Citing this family (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4792621A (en) * 1986-07-28 1988-12-20 Amoco Corporation Method for continuous production of aromatic carboxylic acid
JPH078821B2 (ja) * 1986-09-26 1995-02-01 三井石油化学工業株式会社 芳香族カルボン酸の製造方法
US5068406A (en) * 1989-09-06 1991-11-26 Amoco Corporation Compartmented oxidation method
DE4026733A1 (de) * 1990-08-24 1992-02-27 Huels Chemische Werke Ag Verfahren zur reinigung eines oxidationsabgases
IN182716B (ko) * 1994-03-22 1999-07-03 Mitsui Petrochemical Ind
US5693856A (en) 1996-01-16 1997-12-02 The Boc Group, Inc. Production of terephthalic acid
ID15851A (id) * 1996-02-13 1997-08-14 Mitsubishi Chem Corp Proses untuk menghasilkan suatu asam aromatik karboksilik
US7060853B2 (en) * 2000-01-12 2006-06-13 Invista North America S.A R.L. Method for increasing oxidation reactor production capacity
US6949673B2 (en) * 2000-01-12 2005-09-27 E.I. Du Pont De Nemours And Company Process for producing carboxylic acids
US6657068B2 (en) 2002-03-22 2003-12-02 General Electric Company Liquid phase oxidation of halogenated ortho-xylenes
US6649773B2 (en) 2002-03-22 2003-11-18 General Electric Company Method for the manufacture of halophthalic acids and anhydrides
US6657067B2 (en) 2002-03-22 2003-12-02 General Electric Company Method for the manufacture of chlorophthalic anhydride
US20050256335A1 (en) * 2004-05-12 2005-11-17 Ovidiu Marin Providing gases to aromatic carboxylic acid manufacturing processes
US7541489B2 (en) * 2004-06-30 2009-06-02 Sabic Innovative Plastics Ip B.V. Method of making halophthalic acids and halophthalic anhydrides
US20060004223A1 (en) * 2004-06-30 2006-01-05 General Electric Company Method of making halophthalic acids and halophthalic anhydrides
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 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
US7692036B2 (en) * 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7563926B2 (en) 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 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
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7550627B2 (en) * 2005-03-08 2009-06-23 Eastman Chemical Company Processes for producing aromatic dicarboxylic acids
US20060205974A1 (en) * 2005-03-08 2006-09-14 Lavoie Gino G Processes for producing aromatic dicarboxylic acids
US7884232B2 (en) * 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
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
US8115029B2 (en) * 2006-11-02 2012-02-14 University Of Kansas Cobalt-catalyzed oxidations in volumetrically expanded liquids by compressed gases
CN101279904A (zh) * 2007-04-03 2008-10-08 波克股份有限公司 制造芳族羧酸的改进方法
KR100988684B1 (ko) * 2008-04-16 2010-10-18 삼남석유화학 주식회사 조테레프탈산 제조를 위한 산화 반응기
US20160231034A1 (en) * 2013-10-09 2016-08-11 General Electric Company Water heater with integrated sorption reactor
FR3030539B1 (fr) * 2014-12-17 2018-05-25 Commissariat A L'energie Atomique Et Aux Energies Alternatives Procede de depolymerisation de materiaux polymeres oxygenes
CN108359082A (zh) * 2018-01-23 2018-08-03 浙江省现代纺织工业研究院 一种复合改性对二甲苯的制备方法

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3086993A (en) * 1958-12-31 1963-04-23 Standard Oil Co Liquid phase oxidation process
NL252888A (ko) * 1960-01-30
US3534090A (en) * 1966-11-04 1970-10-13 Mobil Oil Corp Hydrocarbon oxidation
JPS5211875B2 (ko) * 1971-09-16 1977-04-02
GB1395551A (en) * 1971-12-29 1975-05-29 Kanebo Ltd Method of producing polyesters
JPS5291835A (en) * 1976-01-29 1977-08-02 Mitsubishi Chem Ind Ltd Prepation of terephtalic acid for direct polymerization
JPS561301A (en) * 1979-06-20 1981-01-09 Furukawa Electric Co Ltd:The Length measuring device for long magnetic wire

Also Published As

Publication number Publication date
JPH0532381B2 (ko) 1993-05-14
DE3466978D1 (en) 1987-12-03
JPS6036439A (ja) 1985-02-25
KR910006326B1 (ko) 1991-08-20
EP0135341B1 (en) 1987-10-28
EP0135341A1 (en) 1985-03-27
US4593122A (en) 1986-06-03

Similar Documents

Publication Publication Date Title
KR850001723A (ko) p-크실렌으로부터 테레프탈산의 제조방법
GB1462294A (en) Process for producing aromatic carboxylic acids
KR970061848A (ko) 방향족 카르복실산의 제조 방법
US4855492A (en) Process for production of aromatic polycarboxylic acids
MY116843A (en) Production of terephthalic acid
KR840006961A (ko) 직접 중합에 적합한 테레프탈산의 제조방법
KR860003197A (ko) 알킬 방향족 화합물의 액상 산화반응에 의한 방향족 카르복실산의 연속제조방법
US2574644A (en) Recovery of polycarboxylic acid anhydrides
KR950704285A (ko) 3,4-에폭시-1-부텐의 제조방법(method of preparing 3,4-epoxy-1-butene)
CA2222067A1 (en) Effluent gas treatment
KR850001720A (ko) 아크릴산의 제조방법
ES462370A1 (es) Un procedimiento continuo para la produccion de acido teref-talico.
KR880001567A (ko) 방향족 카복실산을 연속적으로 제조하는 방법.
ES475036A1 (es) Procedimiento de preparar continuamente acido tereftalico.
GB1334551A (en) Process for the production of fibre grade terephthalic acid
US4820862A (en) Process for the preparation of dimethyl terephthalate
US4587350A (en) Process for the production of trimellitic anhydride
KR880003892A (ko) 트리멜리트산의 제조방법
US4446070A (en) Catalytic oxidation of polynuclear aromatic hydrocarbons
JPS6012342B2 (ja) テレフタル酸ジメチルエステルの製法
KR900004669A (ko) 이소부틸렌을 산화시켜 메타크롤레인을 생성시키고, 이를 산화시켜 메타크릴산을 생성시키기 위한 무수 희석제
KR860003972A (ko) 이산화탄소의 정제방법
JPS54141721A (en) Preparation of methacrylic acid
KR970065502A (ko) p-크실렌의 산소-기본 산화 반응에서 물 함량을 최적화시키는 방법
GB2194958A (en) Production of synthesis gas

Legal Events

Date Code Title Description
A201 Request for examination
G160 Decision to publish patent application
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20030605

Year of fee payment: 13

EXPY Expiration of term