GB457624A - Continuous process for distilling higher fatty acids - Google Patents
Continuous process for distilling higher fatty acidsInfo
- Publication number
- GB457624A GB457624A GB23867/35A GB2386735A GB457624A GB 457624 A GB457624 A GB 457624A GB 23867/35 A GB23867/35 A GB 23867/35A GB 2386735 A GB2386735 A GB 2386735A GB 457624 A GB457624 A GB 457624A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fatty acids
- steam
- vapours
- liquid
- admitted
- 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
- C11C1/00—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
- C11C1/08—Refining
- C11C1/10—Refining by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
<PICT:0457624/III/1> Fatty acids are purified and distilled by heating the impure material in a heat exchanger 9 under sufficient pressure to maintain it liquid, the liquid being then introduced into a vacuum chamber 1 in which the fatty acids are vaporized substantially instantaneously without additional heat imparted thereto, the vapours being then drawn off and condensed. The escaping vapours first pass through a steam generator 6 the liquefied acid running off into tank 8 and the remaining vapours passing through outlet 7 to a low temperature condenser and a vacuum pump. The heating medium for the exchanger 9 is supplied from a furnace heated liquid heater 10. The steam from generator 6 is superheated in coil 11 and then admitted to chamber 1. Fresh steam may be admitted through connection 26 and surplus steam is drawn off through connection 27. Specification 408,117 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US457624XA | 1935-05-16 | 1935-05-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB457624A true GB457624A (en) | 1936-12-02 |
Family
ID=21939745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB23867/35A Expired GB457624A (en) | 1935-05-16 | 1935-08-26 | Continuous process for distilling higher fatty acids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB457624A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4088542A (en) * | 1975-06-11 | 1978-05-09 | Heinz Schumacher | Method of and device for spontaneously distilling off secondary substances especially from oily liquids |
US4094748A (en) * | 1975-06-16 | 1978-06-13 | Heinz Schumacher | Method of and device for distilling off secondary substances from oily liquids |
-
1935
- 1935-08-26 GB GB23867/35A patent/GB457624A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4088542A (en) * | 1975-06-11 | 1978-05-09 | Heinz Schumacher | Method of and device for spontaneously distilling off secondary substances especially from oily liquids |
US4094748A (en) * | 1975-06-16 | 1978-06-13 | Heinz Schumacher | Method of and device for distilling off secondary substances from oily liquids |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1469447A (en) | Absolute alcohol | |
GB463770A (en) | An improved process for evaporating liquids | |
GB642166A (en) | Improvements in evaporating apparatus | |
GB383570A (en) | Still for substances of high boiling point | |
GB410652A (en) | Process for evaporating, concentrating and distilling | |
GB312089A (en) | Evaporating method and means therefor | |
GB457624A (en) | Continuous process for distilling higher fatty acids | |
GB486415A (en) | Improvements in the distillation of glycerin | |
US3010832A (en) | Method and apparatus for continuous heat-treatment of heat-sensitive liquids | |
GB512657A (en) | Improvements in or relating to method of and apparatus for distillation | |
US2025724A (en) | clendenin | |
GB1501068A (en) | Desalinization distilling plant combined with a steam power plant | |
USRE22775E (en) | Treating fatty acid-containing | |
US1666777A (en) | Method of and apparatus for evaporating and distilling | |
US2701233A (en) | Azeotropic distillation | |
GB546414A (en) | A process of distilling higher fatty acids | |
US1574622A (en) | Process of distilling volatile products | |
GB429720A (en) | Improvements in and relating to the conduct of distillation under high vacuum | |
SU67913A1 (en) | Lactic acid concentration method | |
US2074689A (en) | Combined inert gas recirculation and tar heater operation | |
US1520121A (en) | Process of increasing efficiency of distillation | |
GB883531A (en) | Method of producing an ozonide of an unsaturated fatty acid | |
GB392851A (en) | A plant or still for distilling water or other liquids | |
GB406490A (en) | Improvements in or relating to evaporating and distillation plants heated by compressed vapours | |
GB496677A (en) | Improvements in distillation of high boiling liquids such as fatty acids |