GB486317A - Method of and apparatus for the continuous steam distillation of high boiling point liquids - Google Patents
Method of and apparatus for the continuous steam distillation of high boiling point liquidsInfo
- Publication number
- GB486317A GB486317A GB3332236A GB3332236A GB486317A GB 486317 A GB486317 A GB 486317A GB 3332236 A GB3332236 A GB 3332236A GB 3332236 A GB3332236 A GB 3332236A GB 486317 A GB486317 A GB 486317A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- stage
- still
- stills
- stages
- 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
- C11B3/12—Refining fats or fatty oils by distillation
- C11B3/14—Refining fats or fatty oils by distillation with the use of indifferent gases or vapours, e.g. steam
-
- 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
- C11C1/103—Refining by distillation after or with the addition of chemicals
- C11C1/106—Refining by distillation after or with the addition of chemicals inert gases or vapors
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fats And Perfumes (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
<PICT:0486317/III/1> <PICT:0486317/III/2> In the steam distillation of high boiling liquids, such as fatty acids and glycerine, in two or more serially arranged stages, in at least one of the stages a multiple of the quantity of liquid continuously introduced into the still per unit period is circulated therein and forced up above the surface of the liquid, a portion of the upwardly forced liquid being diverted to the next distillation stage. In a suitable still in which the second distillation stage is effected in an upper annular chamber i, the still is provided with a depending pipe f surrounding a circulation open-ended tube d, which extends into the vapour space of the still, a part of the liquid forced up the tube d by steam admitted at e being trapped by a funnel k and supplied to the chamber i. Each of the stages is both directly and indirectly heated, by perforated pipes g, p and coils c, o respectively. The liquid may be re-cycled to the main still via pipe l and valve s. A number of similar two-stage stills 2, 3, 4 and 11, Fig. 3, may be used in succession in a plant, the stills being connected by feed pipes 8, 9 and 10. Only one of these stills may be of the described type, the others being single-stage stills; the final apparatus 11 may be a condenser in which case the circulation tube is provided with a stirring member 13 and the heating coils replaced by a cooling coil 12. Each of the vessels are connected to a vacuum condenser by pipes 15. In a modification of the invention the two stages of the still are coterminous the liquid of the second stage falling on the surface of the liquid in the first stage a trap being used as before where the liquids meet. Each of the double-stage stills may be connected to a condenser, particularly where fractional distillation is required, as in the separation of the fatty acids in animal and vegetable oils and fats.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3332236A GB486317A (en) | 1936-12-04 | 1936-12-04 | Method of and apparatus for the continuous steam distillation of high boiling point liquids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3332236A GB486317A (en) | 1936-12-04 | 1936-12-04 | Method of and apparatus for the continuous steam distillation of high boiling point liquids |
Publications (1)
Publication Number | Publication Date |
---|---|
GB486317A true GB486317A (en) | 1938-06-02 |
Family
ID=10351443
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3332236A Expired GB486317A (en) | 1936-12-04 | 1936-12-04 | Method of and apparatus for the continuous steam distillation of high boiling point liquids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB486317A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE767827C (en) * | 1939-02-25 | 1953-11-23 | Ig Farbenindustrie Ag | Process for obtaining an oil substitute |
CN112412894A (en) * | 2019-08-23 | 2021-02-26 | 常州市乐萌压力容器有限公司 | Four-stage fractionating type oil diffusion pump with flow distribution plate |
CN114225458A (en) * | 2021-12-25 | 2022-03-25 | 东营威联化学有限公司 | Extractive distillation device for separating aromatic hydrocarbon |
-
1936
- 1936-12-04 GB GB3332236A patent/GB486317A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE767827C (en) * | 1939-02-25 | 1953-11-23 | Ig Farbenindustrie Ag | Process for obtaining an oil substitute |
CN112412894A (en) * | 2019-08-23 | 2021-02-26 | 常州市乐萌压力容器有限公司 | Four-stage fractionating type oil diffusion pump with flow distribution plate |
CN114225458A (en) * | 2021-12-25 | 2022-03-25 | 东营威联化学有限公司 | Extractive distillation device for separating aromatic hydrocarbon |
CN114225458B (en) * | 2021-12-25 | 2022-12-09 | 东营威联化学有限公司 | Extractive distillation device for separating aromatic hydrocarbon |
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