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FR2359634A2 Expired / Lapsed FR ⏱️ 0.0 years remaining

Separating proteins from aq. soln. contg. industrial effluent - by passing through ion exchange resin on mineral support

Assignee: Rhone Poulenc Industries SA
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Filing: 1976-07-28
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Granted: —
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Expires: 1996-07-28
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Abstract

Abstract Process comprises passing a protein soln. though an ion exchange resin. The resin comprises a porous mineral support of 4 mu-k mm particle size, 5-150 m2/g specific surface, 500-2500A degrees pore dia., and 0.4-2 ml/g porous volume. The support is coated with 15 mg/m2 of a cross-linked polymer film contg. or bearing either anion exchange groups which are tert. amines or quaternary ammonium salts or cation exchange acidic groups. The exchange capacity is 2 m equiv./g. The process is used to separate protein from solns. such as lactoserum, beer, blood, body extracts and industrial effluent from abattoirs, the feed and starch industries, providing a purification means for these effluents. Cellulose or dextran ion exchangers used to separate protein are unsuitable for use in a column, undergo volume changes due to ionic force, are biodegradable and cannot be sterilised. The above having none of these disadvantages can be used to obtain very pure protein.

Inventors

  • 👤 Bernard Mirabel
  • 👤 Francois Meiller

Bibliographic Details

Application Number —
Jurisdiction FR
Data Source google_patents
Last Synchronized 2026-11-02 03:25
CPC Classifications
A; A23; A23J; A23J1/00; A23J1/001; A23J1/08; A23J1/16; B; B01; B01J; B01J47/00; B01J47/014; B01J47/016; C; C07; C07K; C07K1/00; C07K1/14; C07K1/16; C07K1/18; C07K16/00; C07K16/06; C07K16/065; C12; C12H; C12H1/00; C12H1/02; C12H1/04; C12H1/0432; C12N; C12N9/00

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