TW200510292A - Process for the purification of a crude carboxylic acid slurry - Google Patents
Process for the purification of a crude carboxylic acid slurryInfo
- Publication number
- TW200510292A TW200510292A TW092134212A TW92134212A TW200510292A TW 200510292 A TW200510292 A TW 200510292A TW 092134212 A TW092134212 A TW 092134212A TW 92134212 A TW92134212 A TW 92134212A TW 200510292 A TW200510292 A TW 200510292A
- Authority
- TW
- Taiwan
- Prior art keywords
- carboxylic acid
- product
- zone
- slurry
- purification
- Prior art date
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
- C07C51/47—Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
-
- 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
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
-
- 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
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
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.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US31529402A | 2002-12-09 | 2002-12-09 | |
US31529502A | 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 |
---|---|
TW200510292A true TW200510292A (en) | 2005-03-16 |
Family
ID=42777809
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW092134212A TW200510292A (en) | 2002-12-09 | 2003-12-04 | 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)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004052821A1 (en) | 2002-12-09 | 2004-06-24 | 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 |
US7390921B2 (en) * | 2004-09-02 | 2008-06-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20060047153A1 (en) * | 2004-09-02 | 2006-03-02 | Wonders Alan G | Optimized liquid-phase oxidation |
EP1786751B1 (en) * | 2004-09-02 | 2015-06-03 | 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 |
US7910769B2 (en) * | 2004-09-02 | 2011-03-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7572936B2 (en) * | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
KR20070048251A (en) * | 2004-09-02 | 2007-05-08 | 이스트만 케미칼 컴파니 | Optimized liquid-phase oxidation |
US7692037B2 (en) | 2004-09-02 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
WO2006028817A2 (en) * | 2004-09-02 | 2006-03-16 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7615663B2 (en) | 2004-09-02 | 2009-11-10 | Eastman Chemical Company | Optimized production of aromatic dicarboxylic acids |
US7399882B2 (en) * | 2004-09-02 | 2008-07-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7683210B2 (en) | 2004-09-02 | 2010-03-23 | Eastman Chemical Company | Optimized liquid-phase oxidation |
MX2007002412A (en) * | 2004-09-02 | 2007-04-23 | Eastman Chem Co | 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 |
US7741515B2 (en) | 2004-09-02 | 2010-06-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7495125B2 (en) * | 2004-09-02 | 2009-02-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
MX336766B (en) * | 2004-09-02 | 2016-01-29 | Grupo Petrotemex Sa De Cv | Optimized production of aromatic dicarboxylic acids. |
LT1791800T (en) * | 2004-09-02 | 2018-01-25 | Grupo Petrotemex, S.A. De C.V. | Optimized liquid-phase oxidation |
CN101518726B (en) * | 2004-09-02 | 2012-12-12 | 奇派特石化有限公司 | Bubble column reactor mainly used for reactions of liquid-phase flow and vapor-phase flow |
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 |
DE102004047076A1 (en) | 2004-09-28 | 2006-04-06 | Zimmer Ag | Process for the preparation of polyesters |
US7557243B2 (en) | 2005-05-19 | 2009-07-07 | Eastman Chemical Company | Enriched terephthalic acid composition |
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 |
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 |
US7741516B2 (en) | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
US7897809B2 (en) | 2005-05-19 | 2011-03-01 | Eastman Chemical Company | Process to produce an enrichment feed |
US20060264664A1 (en) * | 2005-05-19 | 2006-11-23 | Parker Kenny R | Esterification of an exchange solvent enriched composition |
US7834208B2 (en) | 2005-05-19 | 2010-11-16 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US20070179312A1 (en) * | 2006-02-02 | 2007-08-02 | O'meadhra Ruairi Seosamh | Process for the purification of a crude carboxylic axid slurry |
US7420082B2 (en) | 2006-03-01 | 2008-09-02 | Eastman Chemical Company | Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion |
US20070208194A1 (en) * | 2006-03-01 | 2007-09-06 | Woodruff Thomas E | Oxidation system with sidedraw secondary reactor |
US7816556B2 (en) | 2006-03-01 | 2010-10-19 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced multistage oxidative digestion |
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 |
US7772424B2 (en) | 2006-03-01 | 2010-08-10 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion |
US7326807B2 (en) | 2006-03-01 | 2008-02-05 | Eastman Chemical Company | Polycarboxylic acid production system with enhanced heating for 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 |
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)
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 |
WO2004052821A1 (en) * | 2002-12-09 | 2004-06-24 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
-
2003
- 2003-12-03 CA CA002505976A patent/CA2505976A1/en not_active Abandoned
- 2003-12-03 PL PL375595A patent/PL208869B1/en not_active IP Right Cessation
- 2003-12-03 WO PCT/US2003/038305 patent/WO2004052820A1/en active Application Filing
- 2003-12-03 JP JP2005508451A patent/JP2006509044A/en active Pending
- 2003-12-03 KR KR1020057010451A patent/KR101004211B1/en not_active IP Right Cessation
- 2003-12-03 MX MXPA05006046A patent/MXPA05006046A/en active IP Right Grant
- 2003-12-04 TW TW092134212A patent/TW200510292A/en unknown
- 2003-12-05 AR ARP030104500A patent/AR042321A1/en unknown
- 2003-12-06 MY MYPI20034682A patent/MY140391A/en unknown
Also Published As
Publication number | Publication date |
---|---|
PL208869B1 (en) | 2011-06-30 |
JP2006509044A (en) | 2006-03-16 |
PL375595A1 (en) | 2005-12-12 |
CA2505976A1 (en) | 2004-06-24 |
AR042321A1 (en) | 2005-06-15 |
KR101004211B1 (en) | 2010-12-24 |
WO2004052820A1 (en) | 2004-06-24 |
WO2004052820A8 (en) | 2004-09-30 |
MY140391A (en) | 2009-12-31 |
KR20050085478A (en) | 2005-08-29 |
MXPA05006046A (en) | 2005-08-18 |
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