GB908011A - Process for the separation of isophthalic and terephthalic acids - Google Patents
Process for the separation of isophthalic and terephthalic acidsInfo
- Publication number
- GB908011A GB908011A GB3999458A GB3999458A GB908011A GB 908011 A GB908011 A GB 908011A GB 3999458 A GB3999458 A GB 3999458A GB 3999458 A GB3999458 A GB 3999458A GB 908011 A GB908011 A GB 908011A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solution
- acid
- cooling
- acids
- crystals
- 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
- C07C51/42—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
Isophthalic and terephthalic acid are separated from mixtures containing them by forming a solution of them, supersaturating the solution with respect to one of these acids by controlled cooling or concentration so that nucleation is established without substantial precipitation of crystals from the solution, thereafter cooling or concentrating the solution to precipitate the acids as a crystalline mass, and separating from this mass a relatively large-crystal fraction enriched in the nucleated acid, and a relatively small-crystal fraction enriched in the other acid. Preferably the solution is supersaturated with establishment of nucleation by controlled cooling at a slow rate and the subsequent crystallisation is effected by cooling at a relatively rapid rate. The solvent may be water, methanol, ethanol, acetic acid, dimethyl formamide, or dimethyl sulphoxide. The iso- and tere-phthalic acids may be dissolved in hot water under super-atmospheric pressure and the nucleation and crystallisation steps may be effected by evaporatively cooling the solution by reduction in pressure. The treatment may be applied to a mixture of phthalic acids obtained by oxidation of a mixture of xylenes, or other alkyl benzenes or intermediate oxidation products thereof. Such acid mixture may be subjected to solvent extraction to remove orthophthalic acid, and the residue consisting of a mixture of iso- and tere-phthalic acids containing terephthalic acid in excess of that corresponding to the constant solute ratio may be leached with a solvent to form the solution for the separation treatment, leaving a solid residue of terephthalic acid. In an example, water is used as the solvent. A solution of the mixed acids is prepared in an autoclave at 337 DEG F. and is concentrated to effect supersaturation by evaporative cooling. The temperature is lowered slowly to 327 DEG F. and then over a period of 2 hours to 300 DEG F. It is then lowered more rapidly by reducing the pressure to atmospheric pressure over a period of 1/2 to 1 hour. The crystalline mass which is formed is graded by screening using screens of mesh sizes of 35-325. In this way isophthalic acid crystals of 98-94% purity are separated from the smaller crystals in which terephthalic acid predominates. Instead of screening, other methods of grading the crystals may be used e.g. settling, elutriation, and centrifuging. The fractions obtained may be further purified by re-crystallisation, or re-running. Specification 807,091 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US70197057A | 1957-12-11 | 1957-12-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB908011A true GB908011A (en) | 1962-10-10 |
Family
ID=24819394
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3999458A Expired GB908011A (en) | 1957-12-11 | 1958-12-11 | Process for the separation of isophthalic and terephthalic acids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB908011A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998024749A1 (en) * | 1996-12-06 | 1998-06-11 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid |
US5929274A (en) | 1995-06-07 | 1999-07-27 | Hfm International, Inc. | Method to reduce carboxybenzaldehyde isomers in terephthalic acid or isophthalic acid |
US5961935A (en) | 1995-06-07 | 1999-10-05 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid |
US6054610A (en) | 1995-06-07 | 2000-04-25 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid and isophthalic acid from mixed xylenes |
WO2006012287A2 (en) * | 2004-06-28 | 2006-02-02 | Eastman Chemical Company | Method for preparing free-flowing crystalline material |
-
1958
- 1958-12-11 GB GB3999458A patent/GB908011A/en not_active Expired
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5929274A (en) | 1995-06-07 | 1999-07-27 | Hfm International, Inc. | Method to reduce carboxybenzaldehyde isomers in terephthalic acid or isophthalic acid |
US5961935A (en) | 1995-06-07 | 1999-10-05 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid |
US6013835A (en) | 1995-06-07 | 2000-01-11 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid |
US6054610A (en) | 1995-06-07 | 2000-04-25 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid and isophthalic acid from mixed xylenes |
US6113866A (en) | 1995-06-07 | 2000-09-05 | Hfm International, Inc. | Apparatus for preparing purified terephthalic acid |
WO1998024749A1 (en) * | 1996-12-06 | 1998-06-11 | Hfm International, Inc. | Method and apparatus for preparing purified terephthalic acid |
WO2006012287A2 (en) * | 2004-06-28 | 2006-02-02 | Eastman Chemical Company | Method for preparing free-flowing crystalline material |
WO2006012287A3 (en) * | 2004-06-28 | 2006-07-13 | Eastman Chem Co | Method for preparing free-flowing crystalline material |
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