Process for purifying phthalide

Details Process for purifying phthalide Process for purifying phthalide

1998-12-16

1999-10-19

Dentz, Bernard

Organic compounds -- part of the class 532-570 series

Organic compounds

Heterocyclic carbon compounds containing a hetero ring...

C07D30788

Patent

active

059691620

DESCRIPTION:

BRIEF SUMMARY
The present invention relates to a process for purifying a phthalide contaminated by carboxylic acids, carboxylic anhydrides and/or carboxylic esters.
Various syntheses have been described for the preparation of phthalide starting from phthalic acid derivatives. In general, phthalide is prepared by selective hydrogenation of phthalic anhydride (DE-C-28 03 319).
The problem is generally the work-up and purification of the as-synthesized reaction products, since phthalide synthesis almost inevitably produces a crude product contaminated by carboxylic acids and their derivatives such as phthalic acid, phthalic anhydride, monomethyl phthalate, tetrahydrophthalide and 2-methylbenzoic acid. Removal of these by-products is very costly and sometimes not possible just by distillation.
It is known that phthalic anhydride and monomethyl phthalate in particular are not completely removable from phthalide by distillation. If the crude product contains phthalic acid, additional phthalic anhydride is formed during the distillation.
The problems with the removal of by-products mean that phthalide, the product of value, is obtained in only unsatisfactory yield and purity in a distillative work-up.
DE-C-32 45 544 discloses a process for distillative purification of phthalide contaminated by carboxylic acids by admixing the phthalide to be purified with n-butanol or isobutanol prior to the distillation and heating the mixture in an autoclave at between 150 and 280.degree. C. for several hours before subjecting it to a fractional distillation. However, the disadvantages of this procedure are that it is very time-consuming and that excess butanol has to be distilled off prior to the distillation of the phthalide.
It is an object of the present invention to provide a simple and improved process for purifying phthalide essentially contaminated by carboxylic acids and their derivatives.
We have found that this object is advantageously achieved by a process for purifying phthalide contaminated by carboxylic acids, carboxylic anhydrides and/or carboxylic esters, which comprises adding polyethylene glycol and/or polypropylene glycol to the phthalide to be purified and then performing a fractional distillation.
In general, the polyethylene glycol and/or polypropylene glycol is or are added to the phthalide to be purified in amounts from 1 to 50% by weight, advantageously from 2 to 40% by weight, preferably from 3 to 30% by weight, especially from 5 to 15% by weight, particularly advantageously from 8 to 12% by weight, based on phthalide.
It is advantageous to use polyethylene glycol and polypropylene glycol whose average molar mass is within the range from 200 to 600, preferably within the range from 250 to 400.
The polyethylene glycols are advantageously obtained by polyaddition of ethylene oxide to ethylene glycol as initiator molecule in systems usually containing small amounts of water. The polypropylene glycols are formed in a corresponding manner by polyaddition of propylene oxide to 1,2-propanediol as initiator molecule.
It is an advantage of the process of the invention that, in general, even the addition of a relatively small amount of polyethylene glycol or polypropylene glycol to the crude phthalide product is sufficient for the purification process. It is a further advantage of the process that it is possible to dispense with a time-consuming thermal pretreatment of the admixture of crude phthalide and polyethylene glycol or polypropylene glycol. There is no need for prior heating, for example under reflux or in an autoclave. Accordingly, in a preferred embodiment of the purification process, the addition of polyethylene glycol or polypropylene glycol to the crude phthalide is followed by the fractional distillation directly, without further pretreatment. If the chemical structure and the molar mass of the polyethylene glycol or polypropylene glycol are selected in such a way that this ancillary component does not include anything which boils lower than phthalide, phthalide would be one of the low boilers in the distillat

REFERENCES:
patent: 4178295 (1979-12-01), Englaender et al.

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