GB705041A - Improvements in or relating to the continuous refining of fatty oils - Google Patents
Improvements in or relating to the continuous refining of fatty oilsInfo
- Publication number
- GB705041A GB705041A GB12853/52A GB1285352A GB705041A GB 705041 A GB705041 A GB 705041A GB 12853/52 A GB12853/52 A GB 12853/52A GB 1285352 A GB1285352 A GB 1285352A GB 705041 A GB705041 A GB 705041A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- pipe
- lye
- steam
- stage
- 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
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/02—Refining fats or fatty oils by chemical reaction
- C11B3/06—Refining fats or fatty oils by chemical reaction with bases
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Abstract
<PICT:0705041/III/1> In the continuous refining of fatty oils with alkali, the alkali treatment being carried out in two stages and the soap formed in the first stage being separated from the oil before it enters the second stage, steam is blown through the oil during the second stage. The oil is preferably heated to about 100 DEG C. prior to the steam blowing. The oil may be finally washed, dried, bleached and deodorized by blowing with steam under vacuum. In a suitable plant the oil fed to a mixer 2 is neutralized by lye supplied through a pipe 3, and then led to a closed centrifugal separator 5 for removal of the soap formed. The oil is then fed to a mixer 8 and, by supplying steam through a pipe 9, is heated to a temperature of about 100 DEG C. Lye is added to the oil in the mixer 8 from a pipe 10 and the oil then passes to a reaction vessel 12 through which steam is blown from a pipe 13. Dilution of the lye with condensate in the vessel 12 is avoided by heating the oil to about 100 DEG C., and practically all the steam supplied thereto flows therethrough to an outlet 14, producing an intimate mixing of the oil and lye. The oil overflows through a pipe 15 to an open-type centrifugal separator 16 for removal of the freshly formed soap and is discharged through a pipe 18 for subsequent washing, drying, bleaching and deodorizing. Soda lye, potash lye, soda, water glass or mixtures thereof may be used for the second stage of the alkali treatment. The oils specified comprise rape oil, soya-bean oil and fish oil.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE705041X | 1951-06-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB705041A true GB705041A (en) | 1954-03-03 |
Family
ID=20315560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB12853/52A Expired GB705041A (en) | 1951-06-20 | 1952-05-21 | Improvements in or relating to the continuous refining of fatty oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB705041A (en) |
-
1952
- 1952-05-21 GB GB12853/52A patent/GB705041A/en not_active Expired
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