GB308736A - - Google Patents
Info
- Publication number
- GB308736A GB308736A GB9866/29A GB986629A GB308736A GB 308736 A GB308736 A GB 308736A GB 9866/29 A GB9866/29 A GB 9866/29A GB 986629 A GB986629 A GB 986629A GB 308736 A GB308736 A GB 308736A
- Authority
- GB
- United Kingdom
- Prior art keywords
- vapours
- column
- withdrawn
- condensed
- pipe
- 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
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
- B01D1/2803—Special features relating to the vapour to be compressed
- B01D1/2806—The vapour is divided in at least two streams and only a part of the vapour is compressed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
- B01D1/284—Special features relating to the compressed vapour
- B01D1/2856—The compressed vapour is used for heating a reboiler or a heat exchanger outside an evaporator
Abstract
308,736. Distillation Dynamique. March 27, 1928, [Convention date]. Distilling plant and processes; alcoholic liquids, distilling; vapours, utilizing for effecting further evaporation.-In a fractional distillation process of the type in which the vapours are condensed by compression so as to utilize their latent heat, the working pressure in the fractionating column is regulated by the use of heating or cooling means in the column. Crude ethyl alcohol is supplied by a. pipe l to a column b heated by coils c. e. The vapours are withdrawn by a pump a and condensed in the coil c. The condensate passes to a sealed reservoir h from which it is withdrawn through a. float-controlled valve j by a pump d. Part of the condensate is drawn off at p<1> and a regulated amount is refluxed through the pipe t. Air, carbon dioxide, and other gases are withdrawn from the reservoir h through a valve q to a condenser k which returns any condensed vapours by a pipe s to the reflux. The working temperature and pressure of the column b is regulated by a cooling coil g and heating coil e, both of which may be thermostatically controlled by valves f<1>, f. The valve m is opened only when starting the distillation. A number of similar columns may be worked in series,
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR308736T | 1928-03-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB308736A true GB308736A (en) | 1930-05-08 |
Family
ID=31897892
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9866/29A Expired GB308736A (en) | 1928-03-27 | 1929-03-27 |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE561310C (en) |
GB (1) | GB308736A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2487884A (en) * | 1945-12-12 | 1949-11-15 | Little Inc A | Vapor-compression distillation |
US3230155A (en) * | 1960-11-26 | 1966-01-18 | Inventa Ag | Production of pure methanol by thermo-compression distillation |
US3396086A (en) * | 1964-12-23 | 1968-08-06 | Applied Res And Engineering Lt | Recompression evaporators |
US3414484A (en) * | 1966-06-20 | 1968-12-03 | Universal Oil Prod Co | Process for separating ethylbenzene from c8 aromatic hydrocarbons by super-distillation with vapor compression-reboiler heat exchange |
US4615769A (en) * | 1984-04-26 | 1986-10-07 | Nippon Steel Chem. Co., Ltd. | Process for distillation of styrenes |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2629239A (en) * | 1949-08-26 | 1953-02-24 | Universal Oil Prod Co | Separation of closely boiling fractions from a binary mixture |
-
1929
- 1929-03-27 GB GB9866/29A patent/GB308736A/en not_active Expired
- 1929-03-28 DE DES90794D patent/DE561310C/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2487884A (en) * | 1945-12-12 | 1949-11-15 | Little Inc A | Vapor-compression distillation |
US3230155A (en) * | 1960-11-26 | 1966-01-18 | Inventa Ag | Production of pure methanol by thermo-compression distillation |
US3396086A (en) * | 1964-12-23 | 1968-08-06 | Applied Res And Engineering Lt | Recompression evaporators |
US3414484A (en) * | 1966-06-20 | 1968-12-03 | Universal Oil Prod Co | Process for separating ethylbenzene from c8 aromatic hydrocarbons by super-distillation with vapor compression-reboiler heat exchange |
US4615769A (en) * | 1984-04-26 | 1986-10-07 | Nippon Steel Chem. Co., Ltd. | Process for distillation of styrenes |
Also Published As
Publication number | Publication date |
---|---|
DE561310C (en) | 1932-10-13 |
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