GB189136A - Improved continuous process and apparatus for the production of large quantities of absolute alcohol - Google Patents
Improved continuous process and apparatus for the production of large quantities of absolute alcoholInfo
- Publication number
- GB189136A GB189136A GB31258/22A GB3125822A GB189136A GB 189136 A GB189136 A GB 189136A GB 31258/22 A GB31258/22 A GB 31258/22A GB 3125822 A GB3125822 A GB 3125822A GB 189136 A GB189136 A GB 189136A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alcohol
- quicklime
- steam
- heater
- testing
- 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
- B01D3/001—Processes specially adapted for distillation or rectification of fermented solutions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
189,136. Barbet et Fils et Cie, E. Nov. 15, 1921, [Convention date]. Alcohol, dehydrating. -A continuous process for the production of absolute alcohol consists in mixing alcohol of 95-96‹ Gay- Lussac with powdered quicklime or other suitable dyhydrating agent and distilling the greater part in a continuous still, collecting the alcohol, and continuously withdrawing the remaining liquid mixture, diluting it with water and delivering it to a rectifier where it is exhausted of its alcohol which is concentrated to 96‹ and again subjected to dehydration. In the apparatus shown in Fig. 1 lime and alcohol are mixed in a. large stirrer A and delivered by a valve B and pump C to a heater worm JJ and thence to a continuous still E with steam-jacket F and stirrers. The alcohol is condensed in the heater D and cooler G and flows out through a testing- device H. Only about three-quarters of the alcohol are thus distilled, the remaining liquor being continuously tapped off by a pipe e, diluted with water bv a cock S and funnel T and delivered to a continuous exhauster K L, the lower part of which is provided with bubbling plates constructed so as to prevent incrustation with lime. The base M is heated by a steam-bubbler which drives the alcohol into the upper part L of the column, where by means of a reflux N it is rectified to 96‹ and may be withdrawn through a testing-device N<1>, and returned to the apparatus for further dehydration. The calcic mud collecting at the base M is passed into an extractor Q with float q operaing an exit valve R whereby a constant level is maintained in M. In the simpler form of the apparatus shown in Fig. 2, the preliminary reaction between the alcohol and quicklime is dispensed with, the crude alcohol being delivered direct to the upper plate of the column K through a heater X heated by wastesteam from the exhauster K. Pasteurised alcohol is drawn off from the column L by the pipe u to a measuring device U and thence to the still E, E<2> which carries a partition E<1> dividing the unheated portion E from the portion E<2> which is heated by the steam-jacket F. Quicklime is dropped into E in measured quantities by a rotating recessed plug-tap P. It is stated that the testing-device W also serves to separate any aldehyde products. If incomplete dehydration is required the pasteurised alcohol may be drawn off at U. Instead of quicklime, fused calcium chloride, anhydrous potassium carbonate, anhydrous sodium or copper sulphate or anhydrous sodium acetate may be employed.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR189136X | 1921-11-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB189136A true GB189136A (en) | 1923-10-04 |
Family
ID=8878877
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31258/22A Expired GB189136A (en) | 1921-11-15 | 1922-11-15 | Improved continuous process and apparatus for the production of large quantities of absolute alcohol |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB189136A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0107408A2 (en) * | 1982-09-30 | 1984-05-02 | Walter Frank Albers | Process for producing ethanol |
CN113521779A (en) * | 2021-07-21 | 2021-10-22 | 赵慧 | Extraction equipment for mixed alcohol |
CN115575618A (en) * | 2022-09-28 | 2023-01-06 | 广州逆熵电子科技有限公司 | Continuous standard concentration gas generator and use method thereof |
-
1922
- 1922-11-15 GB GB31258/22A patent/GB189136A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0107408A2 (en) * | 1982-09-30 | 1984-05-02 | Walter Frank Albers | Process for producing ethanol |
EP0107408A3 (en) * | 1982-09-30 | 1985-07-03 | Walter Frank Albers | Process for producing ethanol |
CN113521779A (en) * | 2021-07-21 | 2021-10-22 | 赵慧 | Extraction equipment for mixed alcohol |
CN115575618A (en) * | 2022-09-28 | 2023-01-06 | 广州逆熵电子科技有限公司 | Continuous standard concentration gas generator and use method thereof |
CN115575618B (en) * | 2022-09-28 | 2023-08-25 | 广州逆熵电子科技有限公司 | Continuous standard concentration gas generator and use method thereof |
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