CA2248288A1 - Production of aromatic polycarboxylic acids - Google Patents
Production of aromatic polycarboxylic acidsInfo
- Publication number
- CA2248288A1 CA2248288A1 CA002248288A CA2248288A CA2248288A1 CA 2248288 A1 CA2248288 A1 CA 2248288A1 CA 002248288 A CA002248288 A CA 002248288A CA 2248288 A CA2248288 A CA 2248288A CA 2248288 A1 CA2248288 A1 CA 2248288A1
- Authority
- CA
- Canada
- Prior art keywords
- fraction
- carboxylic acid
- aromatic carboxylic
- recycle
- solids
- 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.)
- Granted
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
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Mother liquor, derived from a primary solids-liquid separation process (18) for separating aromatic carboxylic acid crystals from a slurry thereof in the mother liquor, is split into a recycle fraction (30) and a purge fraction (32). the recycle fraction (30) is returned to a reactor (10) in which the aromatic carboxylic acid is formed by liquid phase oxidation of a precursor thereof. The purge fraction (32) is concentrated in evaporator (42) to recover solvent and produce a residue for disposal or further treatment. Before concentration the purge fraction (32), it is subjected to solids-liquid separation in filtration unit (34) to remove fine solids thereby reducing the load on the evaporator (42) and facilitating the recovery of greater amounts of the solvent along with recovery of aromatic carboxylic acid fines, e.g.
for recycle to the reactor (10).
for recycle to the reactor (10).
Applications Claiming Priority (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9603740.3A GB9603740D0 (en) | 1996-02-22 | 1996-02-22 | Production of aromatic polycarboxylic acids |
GB9603740.3 | 1996-02-22 | ||
GB9617994.0 | 1996-08-29 | ||
GBGB9617994.0A GB9617994D0 (en) | 1996-08-29 | 1996-08-29 | Production of aromatic carboxylic acids |
US3327696P | 1996-12-09 | 1996-12-09 | |
US60/033,276 | 1996-12-09 | ||
PCT/GB1997/000439 WO1997030963A1 (en) | 1996-02-22 | 1997-02-18 | Production of aromatic polycarboxylic acids |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2248288A1 true CA2248288A1 (en) | 1997-08-28 |
CA2248288C CA2248288C (en) | 2007-02-06 |
Family
ID=37734912
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002248288A Expired - Fee Related CA2248288C (en) | 1996-02-22 | 1997-02-18 | Production of aromatic polycarboxylic acids |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA2248288C (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008033566A1 (en) * | 2006-09-15 | 2008-03-20 | Eastman Chemical Company | A 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 |
US7741516B2 (en) | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
US7834208B2 (en) | 2005-05-19 | 2010-11-16 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US7855305B2 (en) | 2005-05-19 | 2010-12-21 | Eastman Chemical Company | Process to produce an enriched composition |
US7880031B2 (en) | 2005-05-19 | 2011-02-01 | Eastman Chemical Company | Process to produce an enrichment feed |
US7888529B2 (en) | 2006-03-01 | 2011-02-15 | Eastman Chemical Company | Process to produce a post catalyst removal 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 |
-
1997
- 1997-02-18 CA CA002248288A patent/CA2248288C/en not_active Expired - Fee Related
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
US7741516B2 (en) | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
US7834208B2 (en) | 2005-05-19 | 2010-11-16 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US7855305B2 (en) | 2005-05-19 | 2010-12-21 | Eastman Chemical Company | Process to produce an enriched composition |
US7884231B2 (en) | 2005-05-19 | 2011-02-08 | Eastman Chemical Company | Process to produce an enriched composition |
US7884233B2 (en) | 2005-05-19 | 2011-02-08 | Eastman Chemical Company | Enriched terephthalic acid composition |
US7897809B2 (en) | 2005-05-19 | 2011-03-01 | Eastman Chemical Company | Process to produce an enrichment feed |
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 |
US8053597B2 (en) | 2005-05-19 | 2011-11-08 | Grupo Petrotemex, S.A. De C.V. | Enriched terephthalic acid composition |
US7888529B2 (en) | 2006-03-01 | 2011-02-15 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
WO2008033566A1 (en) * | 2006-09-15 | 2008-03-20 | Eastman Chemical Company | A process to produce an enrichment feed |
Also Published As
Publication number | Publication date |
---|---|
CA2248288C (en) | 2007-02-06 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |