GB726132A - Method of separating liquids by thermal diffusion - Google Patents
Method of separating liquids by thermal diffusionInfo
- Publication number
- GB726132A GB726132A GB14770/53A GB1477053A GB726132A GB 726132 A GB726132 A GB 726132A GB 14770/53 A GB14770/53 A GB 14770/53A GB 1477053 A GB1477053 A GB 1477053A GB 726132 A GB726132 A GB 726132A
- Authority
- GB
- United Kingdom
- Prior art keywords
- feed
- rate
- column
- fraction
- separation
- 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
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/005—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion by thermal diffusion
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Fats And Perfumes (AREA)
Abstract
In separating a liquid into two fractions by thermal diffusion in a column between two walls spaced uniformly apart at 0.01-0.15 inch and maintained at different temperatures, the liquid is introduced at one end of the column, a first fraction is continuously removed at the other end of the column, and a second fraction is continuously removed from the feed end, the ratio of rate of removal of the first fraction to the rate of feed being less than about 1.5:10 by volume. The feed is introduced at the top or bottom of the column adjacent one of the walls and the second fraction is withdrawn adjacent the other wall. The feed rate is preferably at least equal to the normal rate of thermal circulation. Four separation columns may be used in parallel, or two in parallel and the small portions combined and led to a third column from which the large portion is recycled with the main feed. Graphs show the effect on the degree of separation of the small fraction withdrawal rate, the feed rate, and the ratio between these rates. The separation of a petroleum lubricating oil is described and reference is also made to the concentration of stigmasterol from soy bean oil, and the separation of odorous substances from a fish oil.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US726132XA | 1952-06-24 | 1952-06-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB726132A true GB726132A (en) | 1955-03-16 |
Family
ID=22108730
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB14770/53A Expired GB726132A (en) | 1952-06-24 | 1953-05-27 | Method of separating liquids by thermal diffusion |
Country Status (3)
Country | Link |
---|---|
FR (1) | FR1085909A (en) |
GB (1) | GB726132A (en) |
NL (1) | NL179031C (en) |
-
0
- NL NLAANVRAGE7316836,A patent/NL179031C/en active
-
1953
- 1953-05-27 GB GB14770/53A patent/GB726132A/en not_active Expired
- 1953-06-08 FR FR1085909D patent/FR1085909A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
NL179031C (en) | |
FR1085909A (en) | 1955-02-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1251033A (en) | Apparatus for continuous gas-liquid contact and process for refining crude terephthalic acid | |
AR247019A1 (en) | Process for separating hydrocarbon gas constituents | |
US2410583A (en) | Separation of hydrate-forming components of gaseous mixtures | |
DE3262055D1 (en) | Fractionation of fats using a liquefied gas or a gas in the supercritical state | |
ES343487A1 (en) | Gas scrubber | |
US2394968A (en) | Vitamin concentration | |
GB726132A (en) | Method of separating liquids by thermal diffusion | |
US2827172A (en) | Thermal diffusion method and apparatus | |
US2720980A (en) | Thermal diffusion apparatus and method | |
GB380954A (en) | A process of preparing pure components or groups of components from a mixture of liquids | |
GB1194599A (en) | Distillation method and apparatus | |
GB704022A (en) | Method and apparatus for continuous withdrawal of mutually insoluble liquid phases from a settling zone | |
US2508387A (en) | Concentration of vitamin e | |
US2827171A (en) | Thermal diffusion method and apparatus | |
US2454638A (en) | Fractionation of fats | |
GB709660A (en) | Improvements in or relating to method and apparatus for operating a vapor liquid contacting zone | |
GB579761A (en) | Improvements in and relating to continuous separation of sludge and water from raw vegetable and animal oils | |
US2824647A (en) | Thermal diffusion apparatus | |
US2374870A (en) | Vacuum distillation apparatus | |
US2936889A (en) | Rotating thermal diffusion unit and process | |
GB1005087A (en) | Improvements in or relating to the extraction of liquid mixtures | |
GB989341A (en) | Process for the separation of mixtures by means of distillation or absorption | |
US2734633A (en) | Thermal diffusion method | |
GB657715A (en) | Improvements relating to the separation of immiscible liquids | |
ES305014A1 (en) | Procedure of separation of gases of pyrolysis of a wet hydrocarbon. (Machine-translation by Google Translate, not legally binding) |