GB582557A - Improvements in the fractionation of glyceride oils - Google Patents
Improvements in the fractionation of glyceride oilsInfo
- Publication number
- GB582557A GB582557A GB10909/44A GB1090944A GB582557A GB 582557 A GB582557 A GB 582557A GB 10909/44 A GB10909/44 A GB 10909/44A GB 1090944 A GB1090944 A GB 1090944A GB 582557 A GB582557 A GB 582557A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- fraction
- precipitate
- oils
- saturated
- 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
Landscapes
- Fats And Perfumes (AREA)
- Edible Oils And Fats (AREA)
Abstract
Oils of the drying and semi-drying type are fractionated into a fraction more saturated and another fraction more unsaturated than the original oil by mixing the oil with an organic solvent, rapidly chilling the mixture so as to precipitate the more saturated fraction in a flowable form and separating the precipitate in a continuous centrifuge. The precipitate is preferably in an amorphous or very fine crystalline form capable of flowing through the centrifuge for continuous separation as opposed to the ordinary crystalline form separable by filtration which packs or interlocks in the ordinary batch centrifuge. Non-polar solvents are preferred such as petroleum ether, hexane, trichlorethylene and any other hydrocarbons or chlorinated hydrocarbons; polar solvents such as acetone or furfural are less preferred in view of their tendency to produce ordinary crystals but they may be used if the conditions are controlled particularly as to the rate of chilling and the proper degree of agitation so as to minimise crystal formation. In general, 1 part of oil to 1-20 parts of solvent is used. The oil solvent mixture is agitated during the chilling operation, the oil being chilled to a temperature of -20 DEG F. to -60 DEG F. The solvents may be recovered from each of the fractions obtained. The process is particularly adapted for soya bean oil, linseed oil, fish oils, and less usefully for cottonseed oil, the so-called reversion factor of these oils associated with certain odour and taste characteristics being retained in the more unsaturated fraction where it is not objectionable in paints &c. The more saturated fraction is adaptable for edible purposes &c. Specifications 402,651 and 439,128 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US582557XA | 1943-06-23 | 1943-06-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB582557A true GB582557A (en) | 1946-11-20 |
Family
ID=22015652
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10909/44A Expired GB582557A (en) | 1943-06-23 | 1944-06-07 | Improvements in the fractionation of glyceride oils |
Country Status (2)
Country | Link |
---|---|
BE (1) | BE582557A (en) |
GB (1) | GB582557A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2903363A (en) * | 1954-09-17 | 1959-09-08 | Gerald W Farr | Solvent fractionation of winterized cottonseed oil bottoms |
US2942984A (en) * | 1956-04-17 | 1960-06-28 | Lever Brothers Ltd | Edible fats and process of making same |
WO2012016307A1 (en) * | 2010-08-02 | 2012-02-09 | Granol Industria Comércio E Exportaçao Sa | "process for purification of vegetable oils upon withdrawal of solids by centri fugat ion in the miscella stage |
-
1944
- 1944-06-07 GB GB10909/44A patent/GB582557A/en not_active Expired
-
1959
- 1959-09-10 BE BE582557A patent/BE582557A/en unknown
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2903363A (en) * | 1954-09-17 | 1959-09-08 | Gerald W Farr | Solvent fractionation of winterized cottonseed oil bottoms |
US2942984A (en) * | 1956-04-17 | 1960-06-28 | Lever Brothers Ltd | Edible fats and process of making same |
WO2012016307A1 (en) * | 2010-08-02 | 2012-02-09 | Granol Industria Comércio E Exportaçao Sa | "process for purification of vegetable oils upon withdrawal of solids by centri fugat ion in the miscella stage |
CN103189115A (en) * | 2010-08-02 | 2013-07-03 | 格莱诺尔工商贸易出口公司 | Process for purification of vegetable oils upon withdrawal of solids by centri fugat ion in the miscella stage |
US8692004B2 (en) | 2010-08-02 | 2014-04-08 | Granol Industria Comercio E Exportacao Sa | Process for purification of vegetable oils upon withdrawal of solids by centrifugation in the miscella stage |
CN103189115B (en) * | 2010-08-02 | 2015-11-25 | 格莱诺尔工商贸易出口公司 | A kind of the oil water mixture stage by centrifugation remove solid waste with the method for vegetable oil purifying |
Also Published As
Publication number | Publication date |
---|---|
BE582557A (en) | 1959-12-31 |
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