GB1358520A - Oxidation of aromatic organic compounds - Google Patents
Oxidation of aromatic organic compoundsInfo
- Publication number
- GB1358520A GB1358520A GB2609772A GB2609772A GB1358520A GB 1358520 A GB1358520 A GB 1358520A GB 2609772 A GB2609772 A GB 2609772A GB 2609772 A GB2609772 A GB 2609772A GB 1358520 A GB1358520 A GB 1358520A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- oxidation
- oxidation zone
- condensation
- distillation
- 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.)
- Expired
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
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1358520 Aromatic acids K J A CRAMPTON (Institut Francais Du Petrole Des Carburants Et Lubrifiants) 5 June 1972 26097/72 Heading C2C A process for producing a polycarboxylic aromatic acid comprises reacting an aromatic organic compound having at least two oxidizable aliphatic side chains with an oxygen containing gas in the presence of an oxidation catalyst and an inert reaction diluent in a primary oxidation zone, while maintaining a liquid phase in said oxidation zone, and obtaining at least 90% conversion therein, passing the reaction offgases from said oxidation zone to a distillation zone prior to any appreciable condensation of the off-gases, recycling at least a portion of the bottoms of the distillation zone to said oxidation zone, said bottoms containing 1 to 10% by weight of water; conducting the overhead vapour from the distillation zone to a condensation zone, separating effluent from the condensation zone into a liquid stream and a vapour stream containing non-condensable gas, and introducing non-condensable gas, during at least a portion of the period during which oxygen is being substantially completely consumed, into the oxidation zone in an amount sufficient to cause a decrease in the temperature of the oxidation zone of about 5‹ C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2609772A GB1358520A (en) | 1972-06-05 | 1972-06-05 | Oxidation of aromatic organic compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2609772A GB1358520A (en) | 1972-06-05 | 1972-06-05 | Oxidation of aromatic organic compounds |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1358520A true GB1358520A (en) | 1974-07-03 |
Family
ID=10238330
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2609772A Expired GB1358520A (en) | 1972-06-05 | 1972-06-05 | Oxidation of aromatic organic compounds |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1358520A (en) |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0257788A1 (en) * | 1986-07-28 | 1988-03-02 | Amoco Corporation | Process for the continuous production of aromatic carboxylic acid |
WO2002098834A1 (en) * | 2001-06-04 | 2002-12-12 | Eastman Chemical Company | Two stage oxidation process for the production of aromatic dicarboxylic acids |
US7074954B2 (en) | 2002-12-09 | 2006-07-11 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7132566B2 (en) | 2003-09-22 | 2006-11-07 | Eastman Chemical Company | Process for the purification of a crude carboxylic acid slurry |
US7161027B2 (en) | 2002-12-09 | 2007-01-09 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7196215B2 (en) | 2001-06-04 | 2007-03-27 | Eastman Chemical Company | Process for the production of purified terephthalic acid |
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 |
US7342128B2 (en) | 2003-04-25 | 2008-03-11 | Eastman Chemical Company | Method for oxidizing a slurry composition in a post oxidation zone in the presence of added steam |
US7358392B2 (en) | 2002-12-09 | 2008-04-15 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7393973B2 (en) | 2006-03-01 | 2008-07-01 | Eastman Chemical Company | Polycarboxylic acid production system with enhanced residence time distribution for 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 |
US7501537B2 (en) | 2006-03-01 | 2009-03-10 | Eastman Chemical Company | Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange |
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 |
US7829037B2 (en) | 2006-03-01 | 2010-11-09 | Eastman Chemical Company | Oxidation system with sidedraw secondary reactor |
US8455680B2 (en) | 2008-01-15 | 2013-06-04 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
US8614350B2 (en) | 2008-01-15 | 2013-12-24 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
-
1972
- 1972-06-05 GB GB2609772A patent/GB1358520A/en not_active Expired
Cited By (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0257788A1 (en) * | 1986-07-28 | 1988-03-02 | Amoco Corporation | Process for the continuous production of aromatic carboxylic acid |
EP2223908A1 (en) * | 2001-06-04 | 2010-09-01 | Eastman Chemical Company | Two stage oxidation process for the production of aromatic dicarboxylic acids |
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 |
CN100445256C (en) * | 2001-06-04 | 2008-12-24 | 伊士曼化工公司 | Two stage oxidation process for production of aromatic dicarboxylic acids |
WO2002098834A1 (en) * | 2001-06-04 | 2002-12-12 | Eastman Chemical Company | Two stage oxidation process for the production of aromatic dicarboxylic acids |
JP2009263382A (en) * | 2001-06-04 | 2009-11-12 | Eastman Chem Co | Two stage oxidation process for production of aromatic dicarboxylic acid |
JP2013010801A (en) * | 2001-06-04 | 2013-01-17 | Grupo Petrotemex Sa De Cv | Two-stage oxidation process for production of aromatic dicarboxylic acid |
KR100896383B1 (en) * | 2001-06-04 | 2009-05-08 | 이스트만 케미칼 컴파니 | Two stage oxidation process for the production of aromatic dicarboxylic acids |
US7161027B2 (en) | 2002-12-09 | 2007-01-09 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7074954B2 (en) | 2002-12-09 | 2006-07-11 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7358392B2 (en) | 2002-12-09 | 2008-04-15 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
US7342128B2 (en) | 2003-04-25 | 2008-03-11 | Eastman Chemical Company | Method for oxidizing a slurry composition in a post oxidation zone in the presence of added steam |
US7132566B2 (en) | 2003-09-22 | 2006-11-07 | Eastman Chemical Company | Process for the purification of a crude carboxylic acid slurry |
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 |
US7501537B2 (en) | 2006-03-01 | 2009-03-10 | Eastman Chemical Company | Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange |
US7772424B2 (en) | 2006-03-01 | 2010-08-10 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion |
US7393973B2 (en) | 2006-03-01 | 2008-07-01 | Eastman Chemical Company | Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion |
US7816556B2 (en) | 2006-03-01 | 2010-10-19 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced multistage oxidative digestion |
US7829037B2 (en) | 2006-03-01 | 2010-11-09 | Eastman Chemical Company | Oxidation system with sidedraw secondary reactor |
US8153840B2 (en) | 2006-03-01 | 2012-04-10 | Grupo Petrotemex, S.A. De C.V. | 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 |
US7420082B2 (en) | 2006-03-01 | 2008-09-02 | Eastman Chemical Company | Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion |
US8614350B2 (en) | 2008-01-15 | 2013-12-24 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
US8455680B2 (en) | 2008-01-15 | 2013-06-04 | Eastman Chemical Company | Carboxylic acid production process employing solvent from esterification of lignocellulosic material |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |