GB989540A - Interesterification process for fatty glycerides - Google Patents
Interesterification process for fatty glyceridesInfo
- Publication number
- GB989540A GB989540A GB4314561A GB4314561A GB989540A GB 989540 A GB989540 A GB 989540A GB 4314561 A GB4314561 A GB 4314561A GB 4314561 A GB4314561 A GB 4314561A GB 989540 A GB989540 A GB 989540A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alkali metal
- fatty acid
- hydroxide
- free fatty
- glycerol
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Abstract
Fatty glyceride esters containing not more than 0.1% free fatty acid are randomly interesterified by (a) forming a dispersion in the ester of 0.02-0.08%, by weight of the ester, of alkali metal, preferably sodium, hydroxide in the form of a 1-12% aqueous solution containing also at least 0.1%, but preferably not more than 0.3% glycerol, while maintaining the temperature high enough to melt all solids present but not so high as to flash off the glycerol, i.e. generally not above 160 DEG C.; (b) maintaining the temperature at least 120 DEG C. but below that at which the glycerol will boil off, and usually not above 200 DEG C., until the desired degree of molecular rearrangement has been attained; (c) destroying the hydroxide catalyst by addition of an edible acidic material, suitably citric or phosphoric acid, capable of splitting alkali metal soaps, in an amount of 1-5 equivalents of the alkali metal hydroxide present, but preferably in an amount no greater than that which would produce a free fatty acid content in the rearranged esters of 0.7%; and (d) removing the oil-insoluble material thereby formed. If required, steps (a) and/or (b) may be carried out under reduced pressure. If the glycerides to be randomized contain more than 0.1% free fatty acid, they may be pretreated to reduce the level below 0.1% by adding sufficient aqueous alkali metal hydroxide solution containing 1-12% hydroxide, and thereafter removing water by heating under vacuum. Glycerides suitable for interesterification comprises mixture of soyabean oil with tallow or lard, and of palm oil and coconut oil. The free fatty acid present in the product may subsequently be removed by a conventional deodorization process. Specification 802,129 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA812222 | 1960-12-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB989540A true GB989540A (en) | 1965-04-22 |
Family
ID=4141262
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4314561A Expired GB989540A (en) | 1960-12-02 | 1961-12-01 | Interesterification process for fatty glycerides |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB989540A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2594625B1 (en) | 2010-07-16 | 2016-11-16 | Wilmar (shanghai) Biotechnology Research & Development Center Co., Ltd. | Method of controlling level of 3-chloro-1,2-propanediol or esters thereof in oils and fats |
-
1961
- 1961-12-01 GB GB4314561A patent/GB989540A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2594625B1 (en) | 2010-07-16 | 2016-11-16 | Wilmar (shanghai) Biotechnology Research & Development Center Co., Ltd. | Method of controlling level of 3-chloro-1,2-propanediol or esters thereof in oils and fats |
EP2594625B2 (en) † | 2010-07-16 | 2019-12-04 | Wilmar (shanghai) Biotechnology Research & Development Center Co., Ltd. | Method of controlling level of 3-chloro-1,2-propanediol or esters thereof in oils and fats |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES467996A1 (en) | Process for producing lower alcohol esters of fatty acids | |
GB1405346A (en) | Process for the conversion of sterols contained in vegetable and animal oils and fats into their fatty acid esters | |
DE3560167D1 (en) | Process for the production of mixtures of c6-c10 fatty acids | |
JPS5558060A (en) | Preparation of hard butter | |
US2588435A (en) | Process of treating fatty material | |
GB1143143A (en) | Process for vacuum distilling randomly interesterified triglycerides to produce novel triglyceride fractions | |
GB1509664A (en) | Process for refining glyceride oils or fats | |
GB634411A (en) | Method of treating low-grade fatty stock to form alkyl esters therefrom | |
Luddy et al. | Effect of catalytic treatment with sodium methylate on glycerine composition and properties of lard and tallow | |
GB989540A (en) | Interesterification process for fatty glycerides | |
GB1520523A (en) | Processes for the refining of crude oils &c of animal or vegetable origin | |
US3170798A (en) | Interesterification process | |
GB879211A (en) | Improvements in or relating to glyceride esters | |
US2478354A (en) | Preparation of partial esters | |
GB950667A (en) | Process for the preparation of monoglycerides | |
ES397668A1 (en) | Interesterification of glycerides in the presence of an aliphatic ketone | |
GB1025265A (en) | Method of making edible polyglycerol and polyglycerol fatty acid esters | |
GB763474A (en) | Improvements in or relating to the production of fatty acid monoglycerides | |
GB1029237A (en) | Process for preparing a pumpable shortening composition | |
GB160840A (en) | Improvements in the manufacture of nutritious fats | |
GB990401A (en) | Crystallization process | |
GB927965A (en) | Process for the production of lithium soaps of epoxidized fatty acids | |
GB559076A (en) | Improvements in or relating to soap making | |
GB707005A (en) | An improved process for the alcoholysis of glycerides | |
GB1381721A (en) | Interesterification process |