CN201411451Y - Distiller for wine processing - Google Patents
Distiller for wine processing Download PDFInfo
- Publication number
- CN201411451Y CN201411451Y CN200920081720XU CN200920081720U CN201411451Y CN 201411451 Y CN201411451 Y CN 201411451Y CN 200920081720X U CN200920081720X U CN 200920081720XU CN 200920081720 U CN200920081720 U CN 200920081720U CN 201411451 Y CN201411451 Y CN 201411451Y
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- CN
- China
- Prior art keywords
- swort
- interchanger
- pipe
- distiller
- wine
- 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 - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distiller for wine processing, which comprises a distillation tower, a swort heat exchanger and a raw spirit heat exchanger. The distillation tower sequentially comprisesa concentrator, a stripper and a tower kettle from top to bottom; a filtration de-foaming net is arranged between the concentrator and the stripper, a fore-shot outlet is arranged at the top part ofthe concentrator, a feint outlet is arranged on the side wall at the bottom part of the concentrator, and a swort outlet is arranged on the side wall of the swort heat exchanger. The distiller for wine processing further comprises a raw wine flow-out pipe, a swort flow-out pipe, a swort liquid drain pipe and a swort liquid stripping pipe; one end of the raw wine flow-out pipe is connected with theside wall of the concentrator, the other end of the raw wine flow-out pipe is connected with the side wall of the raw spirit heat exchanger, one end of the swort flow-out pipe is connected with the bottom part of the tower kettle, the other end of the swort flow-out pipe is connected with the top part of the swort heat exchanger, one end of the swort liquid stripping pipe is connected with the top part of the raw spirit heat exchanger, and the other end of the swort liquid stripping pipe is connected with the side wall of the stripper. The distiller not only has the advantages of simple as well as reasonable structure, low price, convenient using and the like, but also can makes full use of residual heat, consumes less energy and leads high production efficiency.
Description
Technical field
The utility model relates to the chemical machinery technical field, is specifically related to a kind of novel distiller that is used for drinks processing.
Background technology
Distillation is an important step during liquor is produced.In this step, discriminate distillation by wine and make ethanol and other fragrance matter of wine in cruel be vaporized into wine vapour, again wine vapour is introduced condensing works and produced finished product liquor through the condensation cooling.Water distilling apparatus is discriminated by end pot, wine and condensing works is formed, and the wine Zhen is connected with the inlet of condenser in the condensing works by wine vapour transfer lime, and condensing works is provided with cooling water inlet pipe, rising pipe, and the lower end of condenser is provided with wine outlet duct.
Traditional drinks distiller is to discriminate by steaming, discriminate lid, cross dragon, aluminium matter (plumbous matter) pipe bundle condenser is formed, this kind distiller is batch distillation, energy expenditure is big, distillation efficiency is low, product yield is between 80%-86%, the temperature of going with wine is too high, generally more than 35 ℃, very easily presence of fire accident, and the employing kettle formula that consumption of cooling-water excessive (1 ton of wine water consumption is greater than 18 tons) has abroad distillation, characteristics are directly-firing heating, and this distillation mode has adopted the waste heat of preheating can recovery part wine steam, basically solved the too high problem of energy consumption, but its distillation efficiency and production efficiency thereof do not have much improvement.
The utility model content
The purpose of this utility model is to overcome above-mentioned technical deficiency, a kind of distiller that is used for drinks processing is provided, this distiller that is used for drinks processing not only has advantages such as simple and reasonable, cheap, easy to use, and can make full use of waste heat, less energy consumption, production efficiency height.
For achieving the above object, the technical scheme that the utility model adopted is: a kind of distiller that is used for drinks processing is provided, comprise distillation tower, fermented glutinour rice interchanger and raw spirit interchanger, it is characterized in that: described distillation tower includes thickener from top to bottom successively, carries and heat up in a steamer device and tower still; Described thickener and carrying heats up in a steamer to be provided with between the device to filter to remove indulges in serfing the Net; Described thickener top is provided with foreshot's outlet, and thickener bottom sidewall is provided with the outlet of wine tail; Described fermented glutinour rice interchanger sidewall is provided with the fermented glutinour rice outlet; The described distiller that is used for drinks processing also includes under former wine outlet pipe, fermented glutinour rice outlet pipe, the mash comb and mash and carries and heat up in a steamer pipe; Described former wine outlet pipe one end is connected with the thickener sidewall, and the other end is connected with raw spirit interchanger sidewall; Described fermented glutinour rice outlet pipe one end is connected with tower still bottom, and the other end is connected with fermented glutinour rice interchanger top; Comb one end is connected with raw spirit interchanger bottom under the described mash, and the other end is connected with fermented glutinour rice interchanger sidewall; Described mash is carried and is heated up in a steamer Guan Yiduan and be connected with raw spirit interchanger top, and the other end heats up in a steamer the device sidewall and is connected with carrying.
By top narration as can be seen, the distiller that is used for drinks processing provided by the utility model not only has advantages such as simple and reasonable, cheap, easy to use, and can fully rationally utilize various used heat to save the energy, heat exchange has for the first time utilized institute discharge the heat of the liquid that is pickled with grains or in wine, the heat exchange second time energy recovery that steam is with of filling a wine cup for again; Save water coolant, in second time heat transfer process, mash substitutes water coolant to carry out first time to wine steam and cools off; With respect to batch distillation, greatly improved production efficiency and distillation efficiency, yield rate is up to more than 97%.
Description of drawings
Fig. 1 is the structural representation that is used for the distiller of drinks processing.
Wherein, 1, former wine outlet pipe; 2, filter except that indulging in serfing the Net; 3, foreshot's outlet; 4, thickener; 5, wine tail outlet; 6, carry and heat up in a steamer device; 7, tower still; 8, fermented glutinour rice outlet pipe; 9, fermented glutinour rice outlet; 10, fermented glutinour rice interchanger; 11, comb under the mash; 12, raw spirit interchanger; 13, mash is carried and is heated up in a steamer pipe.
Embodiment
Below in conjunction with accompanying drawing the utility model is further described:
As shown in the figure, this distiller that is used for drinks processing comprises distillation tower, fermented glutinour rice interchanger 10 and raw spirit interchanger 12, and it is characterized in that: described distillation tower includes thickener 4 from top to bottom successively, carries and heat up in a steamer device 6 and tower still 7; Described thickener 4 and carrying heats up in a steamer to be provided with between the device 6 to filter to remove indulges in serfing the Net 2; Described thickener 4 tops are provided with the foreshot and export 3, and thickener 4 bottom sidewalls are provided with wine tail outlet 5; Described fermented glutinour rice interchanger 10 sidewalls are provided with fermented glutinour rice outlet 9; The described distiller that is used for drinks processing also includes under former wine outlet pipe 1, fermented glutinour rice outlet pipe 8, the mash comb 11 and mash and carries and heat up in a steamer pipe 13; Described former wine outlet pipe 1 one ends are connected with thickener 4 sidewalls, and the other end is connected with raw spirit interchanger 12 sidewalls; Described fermented glutinour rice outlet pipe 8 one ends are connected with tower still 7 bottoms, and the other end is connected with fermented glutinour rice interchanger 10 tops; Comb 11 1 ends are connected with raw spirit interchanger 12 bottoms under the described mash, and the other end is connected with fermented glutinour rice interchanger 10 sidewalls; Described mash is carried and is heated up in a steamer pipe 13 1 ends and be connected with raw spirit interchanger 12 tops, and the other end heats up in a steamer device 6 sidewalls and is connected with carrying.
During work, after mash enters distillation tower and distills, last fermented glutinour rice enters into fermented glutinour rice interchanger 10 from tower still 7, because poor liquid has certain heat, thereby can heat the mash that enters in the fermented glutinour rice interchanger 10, mash enters raw spirit interchanger 12 along pipeline then, and be steam at the wine that distillation tower went out, enter raw spirit interchanger 12 from thickener 4 along pipeline and carry out the cooling first time, simultaneously mash is carried out the heating second time, thereby saved a large amount of water coolants, wine is collected then, mash enters to carry and heats up in a steamer device 6 and distill, and so just forms a working cycle.
Though described embodiment of the present utility model in conjunction with the accompanying drawings, the protection domain that those of ordinary skills do not need various distortion that creativity work just can make or modification still to belong to this patent within the scope of the appended claims.
Claims (1)
1, a kind of distiller that is used for drinks processing, the described distiller that is used for drinks processing comprises distillation tower, fermented glutinour rice interchanger (10) and raw spirit interchanger (12), and it is characterized in that: described distillation tower includes thickener (4) from top to bottom successively, carries and heat up in a steamer device (6) and tower still (7); Described thickener (4) and carrying heats up in a steamer to be provided with between the device (6) to filter and removes indulge in serfing the Net (2); Described thickener (4) top is provided with foreshot's outlet (3), and thickener (4) bottom sidewall is provided with wine tail outlet (5); Described fermented glutinour rice interchanger (10) sidewall is provided with fermented glutinour rice outlet (9); The described distiller that is used for drinks processing also includes under former wine outlet pipe (1), fermented glutinour rice outlet pipe (8), the mash comb (11) and mash and carries and heat up in a steamer pipe (13); Described former wine outlet pipe (1) one end is connected with thickener (4) sidewall, and the other end is connected with raw spirit interchanger (12) sidewall; Described fermented glutinour rice outlet pipe (8) one ends are connected with tower still (7) bottom, and the other end is connected with fermented glutinour rice interchanger (10) top; Comb (11) one ends are connected with raw spirit interchanger (12) bottom under the described mash, and the other end is connected with fermented glutinour rice interchanger (10) sidewall; Described mash is carried and is heated up in a steamer pipe (13) one ends and be connected with raw spirit interchanger (12) top, and the other end heats up in a steamer device (6) sidewall and is connected with carrying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920081720XU CN201411451Y (en) | 2009-06-12 | 2009-06-12 | Distiller for wine processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920081720XU CN201411451Y (en) | 2009-06-12 | 2009-06-12 | Distiller for wine processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201411451Y true CN201411451Y (en) | 2010-02-24 |
Family
ID=41713338
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920081720XU Expired - Fee Related CN201411451Y (en) | 2009-06-12 | 2009-06-12 | Distiller for wine processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201411451Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102925333A (en) * | 2012-11-19 | 2013-02-13 | 汪雅平 | Production method of Chinese wolfberry wine |
| CN107299040A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | Multistage distillation brewing device |
| CN117343816A (en) * | 2023-12-04 | 2024-01-05 | 扬州续辉饮料设备有限公司 | Alcohol distillation equipment and alcohol processing technology |
-
2009
- 2009-06-12 CN CN200920081720XU patent/CN201411451Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102925333A (en) * | 2012-11-19 | 2013-02-13 | 汪雅平 | Production method of Chinese wolfberry wine |
| CN107299040A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | Multistage distillation brewing device |
| CN117343816A (en) * | 2023-12-04 | 2024-01-05 | 扬州续辉饮料设备有限公司 | Alcohol distillation equipment and alcohol processing technology |
| CN117343816B (en) * | 2023-12-04 | 2024-03-12 | 扬州续辉饮料设备有限公司 | Alcohol distillation equipment and alcohol processing technology |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100224 Termination date: 20100612 |