GB385866A - Method of and apparatus for distilling substances that are liquid at distillation temperature - Google Patents
Method of and apparatus for distilling substances that are liquid at distillation temperatureInfo
- Publication number
- GB385866A GB385866A GB17239/32A GB1723932A GB385866A GB 385866 A GB385866 A GB 385866A GB 17239/32 A GB17239/32 A GB 17239/32A GB 1723932 A GB1723932 A GB 1723932A GB 385866 A GB385866 A GB 385866A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- pipe
- vapours
- oil
- upcast
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/006—Processes utilising sub-atmospheric pressure; Apparatus therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0385866/III/1> In distilling liquids, e.g. oils, fatty acids, &c. under high vacuum by the injection into the liquid of substances, e.g. steam, which are condensable by cooling with water or air, the latter are injected as propellants into the liquid by means of an upcast pipe of the known gas lift type. Mineral oil boiling above 300 DEG C. in a still 1 is evaporated by injecting, from a pipe 4 into an upcast pipe 3, an oil fraction vaporizing at 200 DEG C. The vaporized light oil carries the heavy oil with it against a baffle 5 and the vapours formed pass off through an outlet 11, the heavy vapours being condensed from the light vapours in a series of condensers. In a modification, the upcast pipe 3 extends into a separate vessel placed above the still. Chemical reactions may be carried out simultaneously with the distillation by the introduction of materials, such as hydrogen peroxide, formaldehyde, &c., with the injected liquid.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE385866X | 1931-06-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB385866A true GB385866A (en) | 1933-01-05 |
Family
ID=6370882
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB17239/32A Expired GB385866A (en) | 1931-06-25 | 1932-06-17 | Method of and apparatus for distilling substances that are liquid at distillation temperature |
Country Status (3)
Country | Link |
---|---|
US (1) | US2018778A (en) |
FR (1) | FR738205A (en) |
GB (1) | GB385866A (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2548015A (en) * | 1947-09-19 | 1951-04-10 | Phillips Petroleum Co | Catalytic hydrogenation and apparatus therefor |
US2774723A (en) * | 1952-10-23 | 1956-12-18 | Phillips Petroleum Co | Vacuum distillation of oils |
US3108049A (en) * | 1958-08-22 | 1963-10-22 | Ici Ltd | Centrifugal apparatus |
US3966559A (en) * | 1973-10-31 | 1976-06-29 | Extraction De Smet | Apparatus for deodorizing oil and similar material |
US4101414A (en) * | 1975-09-02 | 1978-07-18 | Unitech Chemical Inc. | Rerefining of used motor oils |
FR2507097B1 (en) * | 1981-06-04 | 1986-05-09 | Sussmeyer Sprl Ateliers | METHOD AND APPARATUS FOR AUTOMATIC AND CONTINUOUS VAPORIZATION AND CONDENSATION |
US4666587A (en) * | 1983-09-29 | 1987-05-19 | Aaron Seligson | Waste oil purifying process |
US5004850A (en) * | 1989-12-08 | 1991-04-02 | Interstate Chemical, Inc. | Blended gasolines |
US5093533A (en) * | 1989-12-08 | 1992-03-03 | Interstate Chemical, Inc. | Blended gasolines and process for making same |
US5208402A (en) * | 1989-12-08 | 1993-05-04 | Interstate Chemical, Inc. | Liquid fuels for internal combustion engines and process and apparatus for making same |
AU8067891A (en) * | 1990-05-25 | 1991-12-31 | Interstate Chemical Incorporated | Blended gasolines and process and apparatus for making same |
CN109158067A (en) * | 2018-11-07 | 2019-01-08 | 郭继波 | A kind of chemical industry synthesis isomery molecular distillation purification methyl tetrahydro phthalic anhydride process unit |
-
1932
- 1932-06-06 FR FR738205D patent/FR738205A/en not_active Expired
- 1932-06-14 US US617172A patent/US2018778A/en not_active Expired - Lifetime
- 1932-06-17 GB GB17239/32A patent/GB385866A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR738205A (en) | 1932-12-22 |
US2018778A (en) | 1935-10-29 |
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