MY140391A - Process for the purification of a crude carboxylic acid slurry - Google Patents

Process for the purification of a crude carboxylic acid slurry

Info

Publication number
MY140391A
MY140391A MYPI20034682A MYPI20034682A MY140391A MY 140391 A MY140391 A MY 140391A MY PI20034682 A MYPI20034682 A MY PI20034682A MY PI20034682 A MYPI20034682 A MY PI20034682A MY 140391 A MY140391 A MY 140391A
Authority
MY
Malaysia
Prior art keywords
carboxylic acid
product
zone
slurry
purification
Prior art date
Application number
MYPI20034682A
Inventor
Charles Edwan Sumner Jr
David Taylor Bowers
Philip Edward Gibson
Robert Lin
Ernest William Arnold Iii
Eric Jackson Fugate
Geroge M Stevenson
Wayne Mcclanahan
Harry Lee Carrell
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
Priority claimed from US10/645,734 external-priority patent/US7161027B2/en
Priority claimed from US10/645,737 external-priority patent/US7074954B2/en
Priority claimed from US10/667,744 external-priority patent/US7132566B2/en
Application filed by Eastman Chem Co filed Critical Eastman Chem Co
Publication of MY140391A publication Critical patent/MY140391A/en

Links

Classifications

    • 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
    • C07C51/47Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

DISCLOSED IS A PROCESS TO PRODUCE A PURIFIED CARBOXYLIC ACID PRODUCT. THE PROCESS COMPRISES REMOVING IMPURITIES FROM A CRUDE CARBOXYLIC ACID SLURRY IN A SOLID-LIQUID DISPLACEMENT ZONE TO FORM A SLURRY PRODUCT. THE SLURRY PRODUCT IF FURTHER TREATED IN A STAGED OXIDATION ZONE AND A CRYSTALLIZATION ZONE TO FROM A CRYSTALLIZED PRODUCT. THE CRYSTALLIZED PRODUCT IS FURTHER COOLED IN A COOLING ZONE AND SUBSEQUENTLY FILTERED AND DRIED IN A FILTRATION AND DRYING ZONE. THE PROCESS PRODUCES PURIFIED CARBOXYLIC ACID PRODUCT HAVING GOOD COLOR AND LOW IMPURITY LEVELS WITHOUT THE USE OF PURIFICATION STEPS LIKE HYDROGENATION.
MYPI20034682A 2002-12-09 2003-12-06 Process for the purification of a crude carboxylic acid slurry MY140391A (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US31529502A 2002-12-09 2002-12-09
US31529402A 2002-12-09 2002-12-09
US10/645,734 US7161027B2 (en) 2002-12-09 2003-08-21 Process for the oxidative purification of terephthalic acid
US10/645,737 US7074954B2 (en) 2002-12-09 2003-08-21 Process for the oxidative purification of terephthalic acid
US10/667,744 US7132566B2 (en) 2003-09-22 2003-09-22 Process for the purification of a crude carboxylic acid slurry

Publications (1)

Publication Number Publication Date
MY140391A true MY140391A (en) 2009-12-31

Family

ID=42777809

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI20034682A MY140391A (en) 2002-12-09 2003-12-06 Process for the purification of a crude carboxylic acid slurry

Country Status (9)

Country Link
JP (1) JP2006509044A (en)
KR (1) KR101004211B1 (en)
AR (1) AR042321A1 (en)
CA (1) CA2505976A1 (en)
MX (1) MXPA05006046A (en)
MY (1) MY140391A (en)
PL (1) PL208869B1 (en)
TW (1) TW200510292A (en)
WO (1) WO2004052820A1 (en)

Families Citing this family (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL375596A1 (en) 2002-12-09 2005-12-12 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
US7546747B2 (en) 2004-01-15 2009-06-16 Eastman Chemical Company Process for production of a dried carboxylic acid cake suitable for use in polyester production
US20050283022A1 (en) * 2004-06-18 2005-12-22 Sheppard Ronald B Filtrate preparation process for terephthalic acid filtrate treatment
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
WO2006028817A2 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
PL1786751T3 (en) * 2004-09-02 2015-12-31 Grupo Petrotemex Sa De Cv Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
CN102600770B (en) * 2004-09-02 2015-08-19 奇派特石化有限公司 The optimized fabrication of aromatic dicarboxylic acid
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
KR101363824B1 (en) * 2004-09-02 2014-02-17 그루포 페트로테멕스 에스.에이. 데 씨.브이. A bubble column reactor for optimized liquid-phase oxidation
US7683210B2 (en) 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7615663B2 (en) 2004-09-02 2009-11-10 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
CN101022886B (en) * 2004-09-02 2012-05-02 奇派特石化有限公司 Optimized liquid-phase oxidation
EP1786753B1 (en) * 2004-09-02 2015-08-19 Grupo Petrotemex, S.A. De C.V. Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
JP2008511645A (en) * 2004-09-02 2008-04-17 イーストマン ケミカル カンパニー Optimized liquid phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
DE102004047076A1 (en) 2004-09-28 2006-04-06 Zimmer Ag Process for the preparation of polyesters
US7432395B2 (en) 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
US7884231B2 (en) 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
US7897809B2 (en) 2005-05-19 2011-03-01 Eastman Chemical Company Process to produce an enrichment feed
US7880031B2 (en) 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
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
US7741516B2 (en) 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US20060264664A1 (en) * 2005-05-19 2006-11-23 Parker Kenny R Esterification of an exchange solvent 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
US20070179312A1 (en) * 2006-02-02 2007-08-02 O'meadhra Ruairi Seosamh Process for the purification of a crude carboxylic axid slurry
US7772424B2 (en) 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7816556B2 (en) 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7420082B2 (en) 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7326808B2 (en) 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US7888529B2 (en) 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US7393973B2 (en) 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7326807B2 (en) 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system with enhanced heating for oxidative digestion
KR100713253B1 (en) * 2006-04-25 2007-05-02 삼성석유화학(주) Solid and liquid separator in producing terephthalic acid and separating method using the same
KR102070065B1 (en) 2018-03-14 2020-03-02 엘지전자 주식회사 Cyclone type dust collector and Cleaner having the same

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3170768A (en) * 1959-04-22 1965-02-23 Standard Oil Co System for continuous preparation of terephthalic acid
GB2072162B (en) * 1980-03-21 1984-03-21 Labofina Sa Process for the production and the recovery of terephthalic acid
GB9302333D0 (en) * 1993-02-05 1993-03-24 Ici Plc Filtration process
KR970000136B1 (en) * 1993-09-28 1997-01-04 브이.피. 유리예프 Process for producing highly purified benzenedicarboxylic acid isomers
PL375596A1 (en) * 2002-12-09 2005-12-12 Eastman Chemical Company Process for the oxidative purification of terephthalic acid

Also Published As

Publication number Publication date
WO2004052820A1 (en) 2004-06-24
JP2006509044A (en) 2006-03-16
PL208869B1 (en) 2011-06-30
CA2505976A1 (en) 2004-06-24
KR20050085478A (en) 2005-08-29
TW200510292A (en) 2005-03-16
AR042321A1 (en) 2005-06-15
KR101004211B1 (en) 2010-12-24
MXPA05006046A (en) 2005-08-18
PL375595A1 (en) 2005-12-12
WO2004052820A8 (en) 2004-09-30

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