GB604281A - Improvements in or relating to methods of oxidizing relatively long chain unsaturated fatty bodies - Google Patents
Improvements in or relating to methods of oxidizing relatively long chain unsaturated fatty bodiesInfo
- Publication number
- GB604281A GB604281A GB25910/44A GB2591044A GB604281A GB 604281 A GB604281 A GB 604281A GB 25910/44 A GB25910/44 A GB 25910/44A GB 2591044 A GB2591044 A GB 2591044A GB 604281 A GB604281 A GB 604281A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- pelargonic
- per cent
- solution
- acids
- 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
- C11C3/006—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by oxidation
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Relatively long chain unsaturated fatty bodies are oxidized to relatively short chain saturated fatty bodies by treating with a solution made by electrolyzing an aqueous solution containing at least 7 per cent sulphuric acid, and 15-35 per cent chromium sulphate to liberate hydrogen and convert 40-75 per cent of the chromium sulphate to chromic and sulphuric acids. Animal or vegetable oils having substantial unsaturated components, fatty materials having lower unsaturated content, fatty acids obtained from such materials, esters of unsaturated fatty acids, and unsaturated synthetic fatty products may be treated. A preferred oxidizing solution is a 50-60 per cent regenerated solution derived from an original solution containing 1 part chromic anhydride, 2 parts sulphuric acid, and 4 parts water. After use it is again regenerated by electrolysis for re-use. The hydrogen produced may be used to harden other unsaturated fats. The sulphuric acid concentration in the spent solution should not exceed 20 per cent and is 10-15, preferably 12-13 per cent for highest yields and minimum voltage for regeneration. Reaction temperature is usually 5-100 DEG , preferably 75-90 DEG C. The reactants are mixed by stirring and separated by gravity settling or centrifuging, preferably below 40 DEG C. or the separated spent solution is cooled below 40 DEG C. to remove organic material. The oxidizing solution may be added in portions, withdrawal of separated spent solution being effected before addition of the next portion. Oleic acid gives azelaic and pelargonic as well as other shorter chain fatty acids, triolein yields pelargonic acid and mixed glycerides, rape seed oil fatty acids give pelargonic, brassylic and shorter chain acids, while methyl, ethyl, propyl or like esters of oleic acid yield pelargonic acid, the half esters of azelaic acid, and shorter chain fatty acids. The products are treated with sulphuric acid to remove chromium, washed free from acid, and pelargonic acid separated by distillation. The azelaic acid can then be separated from other acids by washing with hot water in such amount that the azelaic content is not above about 10 per cent, and the solution crystallized or evaporated. In examples, a spent solution of percentage composition chromium sulphate 26.9, sulphuric acid 12.2, and water 60.9 is fed to the cathode chambers of a series of continuous cells with lead electrodes and ceramic diaphragms and electrolysed at 24 amps./sq. ft. anode current density to 50 per cent conversion, the solution leaving the anode chambers having the composition: chromic anhydride 6.77, chromium sulphate 13.2, sulphuric acid 21.9, and water 58.1 per cent. This is used for oxidizing: (1) oleic acid, yielding chiefly azelaic and pelargonic acids; (2) cottonseed fatty acids, giving chiefly pelargonic, palmitic and dibasic acids; (3) methyl oleate to pelargonic and azelaic acids and a neutral ester; (4) teaseed oil to pelargonic acid and azelaic acid triglyceride.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US604281XA | 1944-01-20 | 1944-01-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB604281A true GB604281A (en) | 1948-07-01 |
Family
ID=22029408
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25910/44A Expired GB604281A (en) | 1944-01-20 | 1944-12-27 | Improvements in or relating to methods of oxidizing relatively long chain unsaturated fatty bodies |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB604281A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8222438B2 (en) | 2007-05-10 | 2012-07-17 | Novamont S.P.A. | Process for the catalytic cleavage of vegetable oils |
-
1944
- 1944-12-27 GB GB25910/44A patent/GB604281A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8222438B2 (en) | 2007-05-10 | 2012-07-17 | Novamont S.P.A. | Process for the catalytic cleavage of vegetable oils |
US8629290B2 (en) | 2007-05-10 | 2014-01-14 | Novamont S.P.A. | Trigycerides containing certain saturated carboxylic acids |
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