GB698617A - Improved method of separating by distillation the components of aqueous mixtures containing methanol and ethanol - Google Patents
Improved method of separating by distillation the components of aqueous mixtures containing methanol and ethanolInfo
- Publication number
- GB698617A GB698617A GB10708/50A GB1070850A GB698617A GB 698617 A GB698617 A GB 698617A GB 10708/50 A GB10708/50 A GB 10708/50A GB 1070850 A GB1070850 A GB 1070850A GB 698617 A GB698617 A GB 698617A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- methanol
- ethanol
- pipe
- withdrawn
- 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
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/146—Multiple effect distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0698617/III/1> Aqueous ethanol which contains methanol, e.g. a sulphite or sulphate lye, is freed from methanol by a two-stage rectification process; a mixture comprising methanol, water and between 20 to 60 per cent by weight of ethanol is withdrawn as distillate from the first rectification column, and this distillate is then rectified in a second column to strip out the methanol and give aqueous ethanol, free from methanol, as bottoms. An acidic mixture of methanol, water and about 12 per cent ethanol, supplied through pipe 1, is preheated in condenser 6 and then introduced through pipe 2 on to the top plate of column 3 which contains sixteen plates. Column 3 is surmounted by column-section 4 which contains five to seven plates; and neutralizing lye is introduced through pipe 16. Alcohol-free wash is discharged from the sump of column 3 through pipe 5. All the condensate from condensers 6 and 7 is refluxed to section 4, from which a neutral solution containing methanol, water and 25 to 50 per cent of ethanol is withdrawn through pipe 9 and introduced into the side of fractionating-column 10, 11. This column has about 40 plates below the feed-inlet. The condensed distillate from the head of the column, which contains methanol, ethanol and water, is partly returned to the head of the column, and partly withdrawn through line 14. Aqueous ethanol free from methanol, is obtained from the sump of column 10 through pipe 15. The ternary mixture withdrawn from the head of column 11 may be fractionated to give methanol as "heads" and aqueous ethanol as "bottoms"; and the latter may be refluxed to column 10, 11, after adjustment of its composition to ensure that the relative concentration of the ethonal in the total feed to the column, conforms with the invention. Fusel oil and/or other impurities may be withdrawn as a side-stream from column 10, 11.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE698617X | 1949-10-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB698617A true GB698617A (en) | 1953-10-21 |
Family
ID=6608208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10708/50A Expired GB698617A (en) | 1949-10-31 | 1950-05-01 | Improved method of separating by distillation the components of aqueous mixtures containing methanol and ethanol |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB698617A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2826536A (en) * | 1952-12-27 | 1958-03-11 | Pan American Petroleum Corp | Method for purification of ethanol |
FR2508485A1 (en) * | 1981-06-30 | 1982-12-31 | Minas Gerais Siderurg | PROCESS AND INSTALLATION FOR PRODUCING NON-CORROSIVE FUEL ETHYL ALCOHOL |
CN109260748A (en) * | 2018-11-26 | 2019-01-25 | 宁夏北控睿源再生资源有限公司 | A kind of useless methanol production recyclable device and method |
-
1950
- 1950-05-01 GB GB10708/50A patent/GB698617A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2826536A (en) * | 1952-12-27 | 1958-03-11 | Pan American Petroleum Corp | Method for purification of ethanol |
FR2508485A1 (en) * | 1981-06-30 | 1982-12-31 | Minas Gerais Siderurg | PROCESS AND INSTALLATION FOR PRODUCING NON-CORROSIVE FUEL ETHYL ALCOHOL |
CN109260748A (en) * | 2018-11-26 | 2019-01-25 | 宁夏北控睿源再生资源有限公司 | A kind of useless methanol production recyclable device and method |
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