GB908011A - Process for the separation of isophthalic and terephthalic acids - Google Patents

Process for the separation of isophthalic and terephthalic acids

Info

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
Application number
GB3999458A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Co
Original Assignee
Standard Oil Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Standard Oil Co filed Critical Standard Oil Co
Publication of GB908011A publication Critical patent/GB908011A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; 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.
GB3999458A 1957-12-11 1958-12-11 Process for the separation of isophthalic and terephthalic acids Expired GB908011A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (8)

* Cited by examiner, † Cited by third party
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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