CN204874475U - Distillation plant for liquor - Google Patents
Distillation plant for liquor Download PDFInfo
- Publication number
- CN204874475U CN204874475U CN201520471259.4U CN201520471259U CN204874475U CN 204874475 U CN204874475 U CN 204874475U CN 201520471259 U CN201520471259 U CN 201520471259U CN 204874475 U CN204874475 U CN 204874475U
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- still
- stills
- wine
- steam
- kettle
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distillation plant for liquor, including the three stills who establishes ties in proper order, the raw materials passes through the cauldron top entering that feeding pipe followed three stills respectively, and steam passes through the steam pipework and gets into at the bottom of three stills's cauldron respectively, installs steam heating coil at the bottom of the stills cauldron, and steam pipework front end house steward installs first manometer on the road, the wine vapour phase gets into the condenser through wine steam pipe way at the bottom of each other circulating and finally getting into a stills cauldron in the three stills, and three stills's cauldron pushes up the product through ejection of compact pipeline entering condenser. The utility model discloses a continuous still battery, wine vapour are at three cauldron inner loop, and the waste heat of every cauldron of make full use of makes the raw materials that gets into in the stills fully distill energy saving, the liquor taste sweet -smelling of preparing out, adequate quality.
Description
Technical field
The present invention relates to a kind of wine brewing device, be specifically related to a kind of liquor water distilling apparatus.
Background technology
Existing liquor water distilling apparatus generally adopts a larger still kettle to carry out, and its volume is comparatively large, and distill insufficient, and energy consumption is high, UTILIZATION OF VESIDUAL HEAT IN is insufficient, wastes energy, and the wine prepared at utmost can not retain the sweet-smelling of raw material, and mouthfeel is poor.
Summary of the invention
For making up the deficiencies in the prior art, the invention provides a kind of liquor water distilling apparatus of reasonable in design, save energy.
The present invention is achieved through the following technical solutions:
A kind of liquor water distilling apparatus, its special character is: comprise the first still kettle, after-fractionating still and the 3rd still kettle three still kettles of connecting successively, raw material is entered from the still jacking of three still kettles respectively by feeding pipe, steam is entered respectively by vapour line at the bottom of the still of three still kettles, at the bottom of still kettle still, steam heating coil is installed, vapour line front end main pipe rail is provided with the first tensimeter; First still kettle still ejects the wine vapour come and enters at the bottom of after-fractionating still still by the first wine vapor pipeline, after-fractionating still still ejects the wine vapour come and enters at the bottom of the 3rd still kettle still by the second wine vapor pipeline, and the 3rd still kettle still is ejected the wine vapour come and to be entered at the bottom of the first still kettle still by the 3rd wine vapor pipeline and finally enter condenser by wine vapor pipeline; The still top product of three still kettles enters condenser by discharging pipeline.
Liquor water distilling apparatus of the present invention, the raw material entering still kettle is from fermentor tank, and the steam entering still kettle comes from boiler.
Further, liquor water distilling apparatus of the present invention, each still kettle still top is provided with second tensimeter, and the opening for feed of each still kettle is provided with material inlet valve, and discharge port is provided with discharge valve.
Further, liquor water distilling apparatus of the present invention, described three still kettles all adopt copper still, copper resistance to acid is good, can resist the highly acidity of raw wine and be unlikely to still kettle and be corroded, copper as the catalyzer of esterification, can facilitate the synthesis of aromatoising substance simultaneously, remove the S-contained substance harmful to quality, the aromatoising substance comparatively horn of plenty of product.
The invention has the beneficial effects as follows: the present invention adopts three still kettles to carry out continuous still battery, wine vapour is at three still internal recycle, make full use of the waste heat of each still, the raw material entered in still kettle is fully distilled, save energy, accurate control distillation condition, the liquor taste mellow prepared, best in quality.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present invention.
In figure, 1 first still kettle, 2 after-fractionating stills, 3 the 3rd still kettles, 4 feeding pipes, 5 vapour lines, 6 first wine vapor pipelines, 7 second wine vapor pipelines, 8 the 3rd wine vapor pipelines, 9 wine vapor pipelines, 10 discharging pipelines, 11 condensers, 12 steam heating coils, 13 material inlet valves, 14 discharge valves, 15 steam valves, 16 fermentor tanks, 17 boilers, 18 first tensimeters, 19 second tensimeters.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation.
Accompanying drawing is a kind of embodiment of the present invention.This embodiment comprises the first still kettle 1, after-fractionating still 2 and the 3rd still kettle 3 three still kettles of connecting successively, raw material is entered from the still jacking of three still kettles respectively by feeding pipe 4, steam is entered respectively by vapour line 5 at the bottom of the still of three still kettles, steam heating coil 12 is installed at the bottom of still kettle still, vapour line 5 front end main pipe rail is provided with the first tensimeter 18, before steam enters still kettle, control vapor pressure, ensure that distillation pressure-controlling is at 0.01-0.02Mpa.
First still kettle 1 still ejects the wine vapour come and enters at the bottom of after-fractionating still 2 still by the first wine vapor pipeline 6, after-fractionating still 2 still ejects the wine vapour come and enters at the bottom of the 3rd still kettle 3 still by the second wine vapor pipeline 7,3rd still kettle 3 still is ejected the wine vapour come and to be entered at the bottom of the first still kettle 1 still by the 3rd wine vapor pipeline 8 and finally enter condenser 11 by wine vapor pipeline 9, wine vapour fully circulates in three still kettles, ensure distillation efficiency, the still top product of three still kettles enters condenser 11 by discharging pipeline 10, and product flows out bottom condenser 11.
Enter the raw material of still kettle from fermentor tank 16, namely distill workshop section to be connected with fermentation workshop section, steam is from boiler 17, each still kettle still top is provided with second tensimeter 19, wine pressure is steamed in further monitoring, the opening for feed of still kettle is provided with material inlet valve 13, discharge port is provided with discharge valve 14, at the bottom of still, steam inlet place is provided with steam valve 15, three still kettles all adopt copper still, copper resistance to acid is good, the highly acidity of raw wine can be resisted and be unlikely to still kettle and be corroded, copper can as the catalyzer of esterification simultaneously, facilitate the synthesis of aromatoising substance, remove the S-contained substance harmful to quality, the aromatoising substance comparatively horn of plenty of product, make the mouthfeel more sweet-smelling of wine.
Claims (7)
1. a liquor water distilling apparatus, it is characterized in that: comprise the first still kettle (1), after-fractionating still (2) and the 3rd still kettle (3) three still kettles of connecting successively, raw material is entered from the still jacking of three still kettles respectively by feeding pipe (4), steam is entered respectively by vapour line (5) at the bottom of the still of three still kettles, steam heating coil (12) is installed at the bottom of still kettle still, vapour line (5) front end main pipe rail is provided with the first tensimeter (18); First still kettle (1) still ejects the wine vapour come and enters at the bottom of after-fractionating still (2) still by the first wine vapor pipeline (6), the wine vapour that after-fractionating still (2) still ejects enters at the bottom of the 3rd still kettle (3) still by the second wine vapor pipeline (7), and the wine vapour that the 3rd still kettle (3) still ejects is entered at the bottom of the first still kettle (1) still by the 3rd wine vapor pipeline (8) and also finally enters condenser (11) by wine vapor pipeline (9); The still top product of three still kettles enters condenser (11) by discharging pipeline (10).
2. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: raw material is from fermentor tank (16).
3. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: steam is from boiler (17).
4. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: each still kettle still top is provided with second tensimeter (19).
5. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: the opening for feed of each still kettle is provided with material inlet valve (13), and discharge port is provided with discharge valve (14).
6. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: at the bottom of each still kettle still, steam inlet place is provided with steam valve (15).
7. a kind of liquor water distilling apparatus according to claim 1, is characterized in that: described three still kettles adopt copper still.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520471259.4U CN204874475U (en) | 2015-07-03 | 2015-07-03 | Distillation plant for liquor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520471259.4U CN204874475U (en) | 2015-07-03 | 2015-07-03 | Distillation plant for liquor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204874475U true CN204874475U (en) | 2015-12-16 |
Family
ID=54818872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520471259.4U Expired - Fee Related CN204874475U (en) | 2015-07-03 | 2015-07-03 | Distillation plant for liquor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204874475U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106281927A (en) * | 2016-08-26 | 2017-01-04 | 贵州加德邦机械有限公司 | A kind of brandy Distallation systm |
| CN107216986A (en) * | 2017-06-07 | 2017-09-29 | 四川华盛亿科技有限责任公司 | A kind of white wine reprocessing production line and its method |
| WO2019024132A1 (en) * | 2017-08-01 | 2019-02-07 | 张永森 | Distillation system |
| CN113214954A (en) * | 2021-06-17 | 2021-08-06 | 劲牌有限公司 | Distillation device for reducing proportion of white spirit tails and application thereof |
| CN114045198A (en) * | 2021-12-03 | 2022-02-15 | 枣阳市香木瓜技术开发服务中心 | Muskmelon distillation extraction method applied to muskmelon wine |
-
2015
- 2015-07-03 CN CN201520471259.4U patent/CN204874475U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106281927A (en) * | 2016-08-26 | 2017-01-04 | 贵州加德邦机械有限公司 | A kind of brandy Distallation systm |
| CN107216986A (en) * | 2017-06-07 | 2017-09-29 | 四川华盛亿科技有限责任公司 | A kind of white wine reprocessing production line and its method |
| CN107216986B (en) * | 2017-06-07 | 2023-05-02 | 四川华盛亿科技有限责任公司 | White spirit reprocessing production line and method thereof |
| WO2019024132A1 (en) * | 2017-08-01 | 2019-02-07 | 张永森 | Distillation system |
| CN113214954A (en) * | 2021-06-17 | 2021-08-06 | 劲牌有限公司 | Distillation device for reducing proportion of white spirit tails and application thereof |
| CN114045198A (en) * | 2021-12-03 | 2022-02-15 | 枣阳市香木瓜技术开发服务中心 | Muskmelon distillation extraction method applied to muskmelon wine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151216 Termination date: 20180703 |