CN203653528U - Brandy tower type distiller - Google Patents
Brandy tower type distiller Download PDFInfo
- Publication number
- CN203653528U CN203653528U CN201320617510.4U CN201320617510U CN203653528U CN 203653528 U CN203653528 U CN 203653528U CN 201320617510 U CN201320617510 U CN 201320617510U CN 203653528 U CN203653528 U CN 203653528U
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- China
- Prior art keywords
- tower
- brandy
- pot
- still
- distillation tower
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Abstract
The utility model discloses a brandy tower type distiller which is used for distilling brandy. The brandy tower type distiller comprises a distillatory kettle, a kettle cap, a distillation tower, a primary condenser, a secondary condenser and a supporting base, wherein the kettle body and the kettle bottom of the distillatory kettle are of double-layer structures; the sandwich layer of the distillatory kettle can be used for circulating steam; a stirrer and the kettle cap are arranged at the top of the distillatory kettle; the distillation tower and the secondary condenser are connected with the kettle cap by a connecting tube; a three-way ball valve is arranged at a pipeline intersection and used for controlling on and off of the pipeline; the top of the distillation tower is connected with the primary condenser; the secondary condenser is connected with the primary condenser by the connecting tube; and a wine outlet nozzle is connected to the bottom of the secondary condenser. Compared with traditional distillation equipment, the tower type distiller disclosed by the utility model is greatly improved, stronger in practicability, higher in efficiency, wider in scope of application, and capable of providing distilled wine with higher purity.
Description
Technical field
The utility model relates to a kind of distiller, is specially adapted to the tower still of brandy.
Background technology
At present, the brandy water distilling apparatus adopting both at home and abroad, is commonly the Charente distiller of full red copper material, kettle formula distiller and the tower still of all steel material.Adopting red copper material is because copper has good thermal conductivity, the acidity of raw wine is had to good resistance, can make butyric acid, the insoluble mantoquita of formation such as acid, capric acid, lauric acid and separating out, the acid of these unpleasant odors is removed, also can be used as some catalyst for esterification reaction.But the distiller of red copper material also has shortcoming, wine copper content as expensive in material, that distill out is high, have patina taste, and in wine, aromatoising substance easily loses, and dry combustion method etc. easily occurs.Avoid these shortcomings still also to lose the advantage of red copper material although adopt all steel material.In addition, the distillation tower of general tower still is divided into topping still and rectifying tower is two-layer, and in actual production, only has two-layer distillation tower often can not play enough rectification effects.
Utility model content
The utility model will solve the problem of prior art, provide a kind of part-structure to adopt red copper, part-structure adopts stainless steel, and its distillation tower is divided into the novel brandy tower still of four layers, the advantage of existing red copper material, the shortcoming of the red copper material of avoiding again, and the rectifying tower of four layers compares two-layer rectifying tower and has better rectification effect, the wine purity distilling is higher.
A kind of brandy tower still of the present utility model, comprises still pot, pot cap, distillation tower, primary condenser, after-condenser and bearing.Described still pot pot body and the bottom of a pan are bilayer structure, and top is connected with a pot cap, and described distillation tower is connected with pot cap by pipe connecting, distillation tower is divided into four layers, top is connected with primary condenser, and after-condenser is connected with primary condenser by pipe connecting, and after-condenser bottom is provided with beer discharging nozzle.
Wherein, four of described distillation tower layers of column plate are for steeping the formula of covering.
Wherein, at the bottom of the tower that described distillation tower is every layer, be connected with return line, return line is connected with described still pot, between return line and distillation tower and and still pot between ball valve is housed.
Wherein, every one deck tower of described still pot and distillation tower is all equipped with CIP rotating wash bowl.
Wherein, described still pot top is provided with agitator.
Wherein, on the pipe connecting between described still pot and described distillation tower, tee ball valve is housed, wherein two ports are connected with distillation tower with still pot, and the 3rd port is connected with the pipe connecting between described distillation tower and described after-condenser.
Wherein, described beer discharging nozzle bottom is provided with thief hole.
Wherein, described still pot and described pot cap shaped are inverted round stage wide at the top and narrow at the bottom.
Wherein, the material of described pot cap and described distillation tower is red copper, and all the other structure materials of described brandy tower still are stainless steel.
A kind of brandy tower still of the present utility model has following advantage: greatly improved existing brandy distillation plant, can adapt to various Production requirement, improved distillation efficiency and alcohol purity.
Accompanying drawing explanation
Accompanying drawing 1 is the front view of a kind of brandy tower still described in the utility model.
Accompanying drawing 2 is vertical views of a kind of brandy tower still described in the utility model.
Accompanying drawing 3 is structure iron of the distillation tower of a kind of brandy tower still described in the utility model.
1, still pot; 2, pot cap; 3, distillation tower; 4, primary condenser; 5, after-condenser; 6, pipe connecting; 7, CIP rotating wash bowl; 8, column plate; 9, agitator; 10, manhole plate; 11, beer discharging nozzle; 12, thief hole; 13, water-in; 14, water outlet; 15, ball valve; 16, tee ball valve; 17, return line; 18, sewage draining exit; 19, discharge port; 20, steam-in; 21, condensation-water drain; 22, bearing.
Embodiment
Below by embodiment, a kind of brandy tower still of the present utility model is further described.
Embodiment one: first adjust tee ball valve 16 pipe connecting 6 between pot cap 2 and after-condenser 5 is come round, the ball valve 15 on closing volume pipe 17.Open manhole plate 10 and add production desired raw material in still pot 1, shut manhole plate 10, pass into steam toward steam-in 20, open agitator 9 simultaneously, water of condensation a large amount of when beginning flow out from condensation-water drain 21, slowly reduce with temperature rising water of condensation.After being heated to a certain degree, open cooling water system water coolant is flowed into from the water-in 13 of after-condenser 5, flow out from water outlet 14, open thief hole 12.After temperature acquires a certain degree, the various materials in raw material start to evaporate successively and become gas and rise, and enter after-condenser 5 through pot cap 2 and pipe connecting 6, and steam is met condensation and formed liquid, Here it is the former wine alcohol of brandy.Because of foreshot and wine tail impurity more, remove by thief hole 12, middle portion enters storage instrument by beer discharging nozzle 11, and detects alcohol by thief hole 12 sampling in process of production and change.After distillation finishes, steam off, agitator 9 and water coolant, open discharge port 19 remaining tailing flowed out, and opens CIP rotating wash bowl 7 and clean still pot 1, and sewage is flowed out from sewage draining exit 18.
Embodiment two, first adjusts tee ball valve 16 pipe connecting 6 between pot cap 2 and distillation tower 3 is come round, and opens the ball valve 15 on return line 17.Open manhole plate 10 and add production desired raw material in still pot 1, shut manhole plate 10, pass into steam toward steam-in 20, open agitator 9 simultaneously, water of condensation a large amount of when beginning flow out from condensation-water drain 21, slowly reduce with temperature rising water of condensation.After being heated to a certain degree, open cooling water system water coolant is flowed into from the water-in 13 of primary condenser 4 and after-condenser 5, flow out from water outlet 14, open thief hole 12.After temperature acquires a certain degree, various materials in raw material start to evaporate successively become gas rise, enter distillation tower 3 through pot cap 2 and pipe connecting 6, the every column plate 8 through one deck distillation tower 3 of steam, purify to steam in capital, the steam that purity is higher continues to rise, and all the other condense into liquid and get back to still pot 1 by return line 17.Steam condenses into liquid after entering primary condenser 4 and after-condenser 5, Here it is the former wine alcohol of brandy.Because of foreshot and wine tail impurity more, remove by thief hole 12, middle portion enters storage instrument by beer discharging nozzle 11, and detects alcohol by thief hole 12 sampling in process of production and change.After distillation finishes, steam off, agitator 9 and water coolant, open discharge port 19 remaining tailing flowed out, and opens CIP rotating wash bowl 7 and clean still pot 1 and distillation tower 3, and sewage is flowed out from sewage draining exit 18.
Compared with traditional distiller, brandy tower still of the present utility model has following advantage: compared with traditional two-layer distillation tower 3, distillation tower 3 efficiency of four-layer structure are higher, and the alcohol obtaining is purer; The variation of distillation mode, both can simple and easy engler distillation, also can complicated continuous still battery; The production efficiency of raw material is higher, cost-saving, improves output; Local red copper material had both absorbed the advantage of traditional red copper distiller, had alleviated again the shortcoming of red copper material; CIP cleaning system has solved traditional distiller and has cleaned difficult problem.
Claims (9)
1. a brandy tower still, comprise still pot (1), pot cap (2), distillation tower (3), primary condenser (4), after-condenser (5) and bearing (22), it is characterized in that: described still pot (1) pot body and the bottom of a pan are bilayer structure, top is connected with a pot cap (2), described distillation tower (3) is connected with pot cap (2) by pipe connecting (6), distillation tower (3) is divided into four layers, top is connected with primary condenser (4), after-condenser (5) is connected with primary condenser (4) by pipe connecting (6), after-condenser (5) bottom is provided with beer discharging nozzle (11).
2. a kind of brandy tower still according to claim 1, is characterized in that: four layers of column plate (8) of described distillation tower (3) are for steeping the formula of covering.
3. a kind of brandy tower still according to claim 1, it is characterized in that: at the bottom of the tower that described distillation tower (3) is every layer, be connected with return line (17), return line (17) is connected with described still pot (1), between return line (17) and distillation tower (3) and and still pot (1) between ball valve (15) is housed.
4. a kind of brandy tower still according to claim 1, is characterized in that: every one deck tower of described still pot (1) and distillation tower (3) is all equipped with CIP rotating wash bowl (7).
5. a kind of brandy tower still according to claim 1, is characterized in that: described still pot (1) top is provided with agitator (9).
6. a kind of brandy tower still according to claim 1, it is characterized in that: on the pipe connecting (6) between described still pot (1) and described distillation tower (3), tee ball valve (16) is housed, wherein two ports are connected with distillation tower (3) with still pot (1), and the 3rd port is connected with the pipe connecting (6) between described distillation tower (3) and described after-condenser (5).
7. a kind of brandy tower still according to claim 1, is characterized in that: described beer discharging nozzle (11) bottom is provided with thief hole (12).
8. a kind of brandy tower still according to claim 1, is characterized in that: described still pot (1) and described pot cap (2) are shaped as inverted round stage wide at the top and narrow at the bottom.
9. a kind of brandy tower still according to claim 1, is characterized in that: the material of described pot cap (2) and described distillation tower (3) is red copper, and all the other structure materials of described brandy tower still are stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320617510.4U CN203653528U (en) | 2013-10-08 | 2013-10-08 | Brandy tower type distiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320617510.4U CN203653528U (en) | 2013-10-08 | 2013-10-08 | Brandy tower type distiller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203653528U true CN203653528U (en) | 2014-06-18 |
Family
ID=50919940
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320617510.4U Expired - Fee Related CN203653528U (en) | 2013-10-08 | 2013-10-08 | Brandy tower type distiller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203653528U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104818198A (en) * | 2015-04-28 | 2015-08-05 | 温州大宇科技有限公司 | Strong liquor distillation device |
| CN105586231A (en) * | 2016-03-24 | 2016-05-18 | 龙岩市铭威厨房设备有限公司 | Two-time-distillation and two-time-cooling brewing extraction device |
| USD910809S1 (en) * | 2019-04-26 | 2021-02-16 | Next Century Spirits Llc | Alcohol distillation apparatus |
| CN114134005A (en) * | 2021-12-06 | 2022-03-04 | 泰山学院 | Tower type continuous distillation device for brandy |
-
2013
- 2013-10-08 CN CN201320617510.4U patent/CN203653528U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104818198A (en) * | 2015-04-28 | 2015-08-05 | 温州大宇科技有限公司 | Strong liquor distillation device |
| CN104818198B (en) * | 2015-04-28 | 2017-01-25 | 温州大宇科技有限公司 | Strong liquor distillation device |
| CN105586231A (en) * | 2016-03-24 | 2016-05-18 | 龙岩市铭威厨房设备有限公司 | Two-time-distillation and two-time-cooling brewing extraction device |
| USD910809S1 (en) * | 2019-04-26 | 2021-02-16 | Next Century Spirits Llc | Alcohol distillation apparatus |
| CN114134005A (en) * | 2021-12-06 | 2022-03-04 | 泰山学院 | Tower type continuous distillation device for brandy |
| CN114134005B (en) * | 2021-12-06 | 2023-08-29 | 泰山学院 | Brandy tower type continuous distillation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent for invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Liu Budan Inventor after: Hu Shaowu Inventor before: Liu Budan Inventor before: Hu Shaowu |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140618 Termination date: 20151008 |
|
| EXPY | Termination of patent right or utility model |