SU825623A1 - Apparatus for producing raw alcohol from yeast precipitate - Google Patents
Apparatus for producing raw alcohol from yeast precipitate Download PDFInfo
- Publication number
- SU825623A1 SU825623A1 SU792772884A SU2772884A SU825623A1 SU 825623 A1 SU825623 A1 SU 825623A1 SU 792772884 A SU792772884 A SU 792772884A SU 2772884 A SU2772884 A SU 2772884A SU 825623 A1 SU825623 A1 SU 825623A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- alcohol
- producing raw
- raw alcohol
- yeast
- yeast precipitate
- Prior art date
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
(54) АППАРАТ ДЛЯ ПОЛУЧЕНИЯ СПИРТАСЫРЦА ИЗ ДРОЖЖЕВЫХ. ОСАДКОВ(54) THE APPARATUS FOR RECEIVING AN ALCOHOL FROM THE YEAST. DROP
ной части, холодильником 10, служащим дл конденсации водно-спиртовых паров, и системой трубопроводовpart, a cooler 10, used to condense water-alcohol vapors, and a piping system
При этом кажда секци аппарата представл ет собой трубу 11 с крышками 12 и патрубками 5, внутри которой установлен вал б с тарелками 7, причем концы вала 6 фи{ссируютс на крышках 12 в квадратных гнездах 13. При необхбдимости очистки какой-либ секции 2 снимаетс нижн крышка 1 и вс внутренн конструкци , вал 6 с тарелками 7, вынимаетс из секцииAt the same time, each section of the apparatus is a pipe 11 with lids 12 and nozzles 5, inside which is mounted a shaft 6 with plates 7, and the ends of the shaft 6 are fit on the lids 12 in square slots 13. If it is necessary to clean any section 2, it is removed the bottom cover 1 and the entire internal structure, the shaft 6 with the plates 7, is removed from the section
Аппарат работает следующим образом .The device works as follows.
Жидкие дрожжевые осадки подаютс насосом на чертеже не повазан) через патрубок Холодные дрожжевые осадки в трубное пространство дефлегматора 9, подогреваютс там за счет тепла водно-спиртовых паров, движущихс навстречу в межтрубном пространстве, и по трубе 14 переход т в истощающую часть 3, пройд которую, переход т в выварной куб 1 где окончательно освобождаютс от спирта и вывод тс в виде барды через патрубок Барда.Liquid yeast sediments are pumped into the drawing (not spoiled) through the branch pipe. Cold yeast sediments into the pipe space of the reflux condenser 9, are heated there by the heat of water-alcohol vapor moving towards the annular space, and through the pipe 14 are transferred to exhaustive part 3, which passes The transition into the boiled cube 1 where it is finally freed from alcohol and output as bards through the Bard pipe.
В выварной куб 1 аппарата подаетс пар, который движетс навстречу дроиокевым осадкам, выварива из ник спирт в выварном кубе 1 и истощающей части 3. В укрепл ющей части-4 водно-спиртова смесь частично конденсируетс и стекает в истощающую часть, а более крепкие пары, пройд укрепл ющую часть 4 по труб 15, поступают в межтрубное пространство дефлегматора 9, Здесь также происходит частична конденсаци водноспиртовых паров, при этом конденсат в виде флегм по трубе 16 возвращаетс в верхнюю секцию 2 укрепл ющей части 4. Крепкие водно-спиртовые пары с концентрацией спирта 75-78 об.%., пройд дефлегматор 9 по трубе 17, поступают в холодильник 10, где окончательно конденсируютс и выход т в виде готового продукта - спирта-сырца.In the boiled cube 1 of the apparatus, steam is supplied, which moves towards the precipitate, digest the alcohol in the boiled cube 1 and the depleting part 3. In the strengthening part-4, the water-alcohol mixture partially condenses and flows into the exhaustive part, and the stronger pairs, having passed the strengthening part 4 through pipes 15, enter the annular space of the dephlegmator 9, here also partial condensation of hydroalcoholic vapors occurs, while condensate in the form of reflux through the pipe 16 returns to the upper section 2 of the strengthening part 4. Strong water-alcohol .. Couples with an alcohol concentration of 75-78 vol%, the reflux condenser 9 after passing through the tube 17, fed into the refrigerator 10, where finally condensed and exit in the form of finished product - crude alcohol.
Предлагаемый аппарат дл получени спирта-сырца из дрожжевых осадков обеспечивает улучшение условий его эксплуатации.The proposed apparatus for obtaining raw alcohol from yeast sediments provides an improvement in its operating conditions.
1515
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU792772884A SU825623A1 (en) | 1979-04-16 | 1979-04-16 | Apparatus for producing raw alcohol from yeast precipitate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU792772884A SU825623A1 (en) | 1979-04-16 | 1979-04-16 | Apparatus for producing raw alcohol from yeast precipitate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU825623A1 true SU825623A1 (en) | 1981-04-30 |
Family
ID=20830575
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU792772884A SU825623A1 (en) | 1979-04-16 | 1979-04-16 | Apparatus for producing raw alcohol from yeast precipitate |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU825623A1 (en) |
-
1979
- 1979-04-16 SU SU792772884A patent/SU825623A1/en active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SU825623A1 (en) | Apparatus for producing raw alcohol from yeast precipitate | |
| GB1493045A (en) | Heat exchanger | |
| JPS56113717A (en) | Distillation device for alcohol | |
| GB486415A (en) | Improvements in the distillation of glycerin | |
| CN209307296U (en) | A kind of system that tri-mixed fractions are adopted in tar vacuum distillation | |
| US1559218A (en) | Process of continuous rectification of spirits, petroleums, and benzols | |
| SU23315A1 (en) | Dephlegmator | |
| RU87363U1 (en) | SMALL APPARATUS FOR PRODUCING PURE ETHYL ALCOHOL AND DISTILLED WATER | |
| JPH0634801Y2 (en) | Distillation equipment | |
| RU2058382C1 (en) | Unit for production of rectified alcohol | |
| RU2022608C1 (en) | Fractioning tower for separation of hydrocarbon mixtures | |
| RU41639U1 (en) | INSTALLATION FOR VACUUM RECTIFICATION OF LIQUID MIXTURES | |
| JPS5784701A (en) | Method for concentrating fermented liquor and separating alcohol by evaporation | |
| SU35843A1 (en) | Device for dry distillation of wood | |
| RU2067108C1 (en) | Plant for production of bitumens and fuel from heavy oil | |
| SU800189A2 (en) | Method of producing brendy alcohol | |
| JPS54103403A (en) | Treatment of waste oil | |
| SU46669A1 (en) | Superheated Steam Steaming Method | |
| GB239208A (en) | Improvements in and relating to vapour separation and condensation particularly for use with oils | |
| SU863635A1 (en) | Method of concentrating food vinegar | |
| SU16191A1 (en) | Apparatus for increasing circulation in evaporator heating tubes | |
| RU1822868C (en) | Plant for production of rectified alcohol | |
| SU67913A1 (en) | Lactic acid concentration method | |
| SU390139A1 (en) | DEVICE OF CONTINUOUS ACTION FOR OBTAINING COGAR ALCOHOL | |
| GB368838A (en) | Improvements relating to the distillation of hydrocarbons and apparatus therefor |