GB1152577A - Purification of Aromatic Polycarboxylic Acids. - Google Patents
Purification of Aromatic Polycarboxylic Acids.Info
- Publication number
- GB1152577A GB1152577A GB2165666A GB2165666A GB1152577A GB 1152577 A GB1152577 A GB 1152577A GB 2165666 A GB2165666 A GB 2165666A GB 2165666 A GB2165666 A GB 2165666A GB 1152577 A GB1152577 A GB 1152577A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- aromatic polycarboxylic
- purified
- polycarboxylic acids
- terephthalic
- 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
- 239000002253 acid Substances 0.000 title abstract 7
- 125000003118 aryl group Chemical group 0.000 title abstract 4
- 150000007513 acids Chemical class 0.000 title abstract 3
- 238000000746 purification Methods 0.000 title abstract 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 abstract 4
- 239000003054 catalyst Substances 0.000 abstract 2
- 238000005984 hydrogenation reaction Methods 0.000 abstract 2
- 239000007791 liquid phase Substances 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 abstract 1
- 238000010923 batch production Methods 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 238000010924 continuous production Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 239000000706 filtrate Substances 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical class C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 239000002798 polar solvent Substances 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
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
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,152,577. Purification of aromatic polycarboxylic acids. STANDARD OIL CO. 16 May, 1966 [17 May, 1965], No. 21656/66. Addition to 994,769. Heading C2C. An aromatic polycarboxylic acid containing undesirable aldehyde and other impurities is purified by a process which comprises contacting a solution of the impure acid in demineralized water in the liquid phase at an elevated temperature and pressure and in the presence of H 2 with a Pd-containing catalyst under mild hydrogenation conditions, and recovering purified acid. The aromatic polycarboxylic acid may be obtained by liquid phase catalytic oxidation of polyalkyl aromatic hydrocarbons. Specified polycarboxylic acids which may be purified are terephthalic, isophthalic, trimesic, trimellitic, mellitic and naphthalene dicarboxylic acids. The hydrogenation is suitably carried out at a temperature in the range of about 450-600‹ F., in an inert polar solvent either as a batch process under static conditions or as a continuous process maintaining a concurrent or countercurrent flow of H 2 through the catalyst chamber. A sufficient pressure may be maintained in a reactor by using a mixture of H 2 and an inert gas, e.g. N 2 . The product may be obtained from the reaction mixture by filtering and crystallizing from the filtrate. A process is described with reference to the accompanying drawings (not shown) for the preparation of terephthalic acid. Examples are given for the production of terephthalic acid showing the effect of using water of varying purity.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US45621465A | 1965-05-17 | 1965-05-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1152577A true GB1152577A (en) | 1969-05-21 |
Family
ID=23811917
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2165666A Expired GB1152577A (en) | 1965-05-17 | 1966-05-16 | Purification of Aromatic Polycarboxylic Acids. |
Country Status (8)
| Country | Link |
|---|---|
| AT (1) | AT288360B (en) |
| BE (1) | BE681178A (en) |
| CH (1) | CH448048A (en) |
| DE (1) | DE1593539B2 (en) |
| ES (1) | ES326851A1 (en) |
| GB (1) | GB1152577A (en) |
| NL (1) | NL6606728A (en) |
| SE (1) | SE344741B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0206715A3 (en) * | 1985-06-17 | 1988-09-07 | Amoco Corporation | Purification of terephthalic acid |
| WO2003053904A3 (en) * | 2001-12-20 | 2003-12-18 | Bp Corp North America Inc | Purification of a crude acid mixture |
| WO2005070862A3 (en) * | 2004-01-15 | 2005-09-22 | Eastman Chem Co | Process for production of a dried carboxylic acid cake suitable for use in polyester production |
| 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 |
| US7358392B2 (en) | 2002-12-09 | 2008-04-15 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
| 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 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58126834A (en) * | 1982-01-23 | 1983-07-28 | Mitsubishi Gas Chem Co Inc | Crystallization method of trimellitic acid |
-
1966
- 1966-05-16 GB GB2165666A patent/GB1152577A/en not_active Expired
- 1966-05-17 SE SE685666A patent/SE344741B/xx unknown
- 1966-05-17 NL NL6606728A patent/NL6606728A/xx unknown
- 1966-05-17 CH CH712866A patent/CH448048A/en unknown
- 1966-05-17 ES ES0326851A patent/ES326851A1/en not_active Expired
- 1966-05-17 BE BE681178D patent/BE681178A/xx unknown
- 1966-05-17 DE DE1966ST025410 patent/DE1593539B2/en active Granted
- 1966-05-17 AT AT466566A patent/AT288360B/en not_active IP Right Cessation
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0206715A3 (en) * | 1985-06-17 | 1988-09-07 | Amoco Corporation | Purification of terephthalic acid |
| WO2003053904A3 (en) * | 2001-12-20 | 2003-12-18 | Bp Corp North America Inc | Purification of a crude acid mixture |
| 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 |
| US7132566B2 (en) | 2003-09-22 | 2006-11-07 | Eastman Chemical Company | Process for the purification of a crude carboxylic acid slurry |
| WO2005070862A3 (en) * | 2004-01-15 | 2005-09-22 | Eastman Chem Co | Process for production of a dried carboxylic acid cake suitable for use in polyester production |
| JP2007517896A (en) * | 2004-01-15 | 2007-07-05 | イーストマン ケミカル カンパニー | Process for producing a dry carboxylic acid cake suitable for use in polyester production |
| 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 |
| RU2380352C2 (en) * | 2004-01-15 | 2010-01-27 | Истман Кемикал Компани | Method of preparing dry residue of carboxylic acid suitable for synthesis of polyesters |
| EP2450342A3 (en) * | 2004-01-15 | 2013-10-23 | Grupo Petrotemex, S.A. De C.V. | Process for production of a dried carboxylic acid cake suitable for use in polyester production |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| AT288360B (en) | 1971-03-10 |
| SE344741B (en) | 1972-05-02 |
| NL6606728A (en) | 1966-11-18 |
| ES326851A1 (en) | 1967-07-01 |
| CH448048A (en) | 1967-12-15 |
| BE681178A (en) | 1966-10-31 |
| DE1593539B2 (en) | 1977-03-10 |
| DE1593539A1 (en) | 1970-12-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed | ||
| PE | Patent expired |