Organic compounds -- part of the class 532-570 series – Organic compounds – Heterocyclic carbon compounds containing a hetero ring...
Patent
1990-05-24
1991-08-13
Springer, David B.
Organic compounds -- part of the class 532-570 series
Organic compounds
Heterocyclic carbon compounds containing a hetero ring...
548555, C07D207267
Patent
active
050398172
DESCRIPTION:
BRIEF SUMMARY
The present invention relates to a process for the preparation of pure N-vinyl-2-pyrrolidone ("vinylpyrrolidone").
Vinylpyrrolidone is an important monomer for the preparation of copolymers and, especially, homopolymers, which in turn are used, for example, in medicine as plasma expanders and in cosmetics as hair fixatives. Crosslinked polyvinylpyrrolidone (polyvinylpolypyrrolidone) is used inter alia for clarifying beverages, mainly beer.
For these purposes the polymers must meet very high purity requirements, so that even the monomer must be prepared in high purity. However, the latter gives rise to considerable difficulties because the conventional synthesis from 2-pyrrolidone and acetylene produces vinylpyrrolidone containing basic substances, as is evident from the fact that a 10% by weight aqueous solution of vinylpyrrolidone, which is intrinsically neutral, has a pH of about 9 to 10.
Although vinylpyrrolidone can be purified by distillation (Ullmanns Enzyklopadie der Technischen Chemie, 4th edition, volume 23 (1983), page 611), the purifying effect achievable thereby with normal technical resources is insufficient. More extensive purification is associated with longer exposure of vinylpyrrolidone to heat, which leads to partial polymerization thereof and, consequently, considerable technical problems with distillation, to say nothing of the losses of vinylpyrrolidone.
Furthermore, DE-A 224 23 607 discloses the removal of polar compounds, including N-methylpyrrolidone, from liquid hydrocarbons using acid ion exchangers and, additionally, DE-A 11 71 435 and Chem. Abstr. volume 88, 1978, Abstract 50 675 m describe the purification of caprolactam using acid ion exchangers. However, these publications say nothing about treatment of N-vinyl-2-pyrrolidone, which is a highly sensitive chemical, with acidic resins.
The object of the present invention was therefore to obtain vinylpyrrolidone in highly pure form while avoiding the disadvantages described.
Accordingly, we have found a process for the preparation of pure N-vinyl-2-pyrrolidone, which comprises treating the crude N-vinyl-2-pyrrolidone with an acid ion exchanger.
Particularly suitable crude vinylpyrrolidone is that obtainable by reaction of pyrrolidone with acetylene in the presence of strong basic catalysts such as N-alkali-metal-pyrrolidones (Reppe process, see Ullmann loc. cit.). The nature of the basic impurities which are produced by this and are evident from an increase in the pH of aqueous vinylpyrrolidone solutions is unknown, but this is immaterial to the process according to the invention. It is advisable initially to purify by distillation the crude vinylpyrrolidone produced in the synthesis, before it is further treated in the manner according to the invention. The concentration of basic substances in the product purified in this way is about 200 to 500 ppm.
Suitable acid ion exchangers are acidified inorganic materials of this type, e.g. zeolites, but especially resins with carboxyl, sulfo or phosphono groups as acid groups. The resins which have the greatest importance in practice are crosslinked vinyl polymers because they are very chemically stable, contain or release virtually no impurities and can be regenerated many times.
Resins of this type are known under their proprietary names such as Amberlite.RTM., Dowex.RTM., Lewatit.RTM. and Wofatit.RTM., with further designations providing information on the specific properties in each case.
In general, weakly acidic to moderately strongly acidic resins which contain carboxyl or sulfo groups are preferred to strongly acidic resins containing sulfo groups because strongly acidic resins may initiate polymerization of the vinylpyrrolidone.
Examples of suitable acid ion exchangers (cation exchangers) are Lewatit CNP 80 and CNP LF and Amberlite IRC-84, IRC-84 F 6, IRC-72 and IRC-50.
Since the exchanger resins are not exposed to particular thermal or chemical stress in the process according to the invention, and since they do not have to meet any specific selectivity requirements either, it i
REFERENCES:
patent: 4276215 (1981-06-01), Hart et al.
Hofmann Ernst
Kroker Ruprecht
Mueller Guenther
BASF - Aktiengesellschaft
Springer David B.
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