CN103194364B - Distiller - Google Patents
Distiller Download PDFInfo
- Publication number
- CN103194364B CN103194364B CN201310154554.2A CN201310154554A CN103194364B CN 103194364 B CN103194364 B CN 103194364B CN 201310154554 A CN201310154554 A CN 201310154554A CN 103194364 B CN103194364 B CN 103194364B
- Authority
- CN
- China
- Prior art keywords
- condenser
- preheater
- foreshot
- pot
- valve
- 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
Links
- HWJPHQNEWARZLH-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,5,5-decafluoro-6,6-bis(trifluoromethyl)cyclohexane Chemical compound FC(F)(F)C1(C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F HWJPHQNEWARZLH-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000003517 fume Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 21
- 244000261422 Lysimachia clethroides Species 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 6
- 230000035622 drinking Effects 0.000 claims description 5
- 235000013532 brandy Nutrition 0.000 abstract description 11
- 238000004821 distillation Methods 0.000 abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 8
- 230000001476 alcoholic effect Effects 0.000 description 7
- 239000000446 fuel Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a distiller which is particularly applicable to distillation of brandy, and belongs to the technical field of distiller structures. The distiller comprises a first distillatory pot and a second distillatory pot which are provided with heating devices, a preheater mounted above the second distillatory pot, and a foreshot condenser used for condensing low-degree wine fume, wherein the first distillatory pot, the second distillatory pot, the preheater and the foreshot condenser are communicated by pipelines provided with dump valves; a first return device and a second return device are mounted on the first distillatory pot and the preheater respectively, and are communicated with the second distillatory pot and the foreshot condenser through pipelines respectively; a wine fume return pipe communicated with the second distillatory pot is mounted in the preheater; a feed valve is mounted on the preheater; a condenser used for condensing high-degree wine fume is mounted below the foreshot condenser; and a wine measuring device and a water inlet valve are mounted on the condenser. The distiller is reasonable in structural design and convenient to use, and the original brandy with the alcohol concentration above 60% can be prepared by once distillation.
Description
Technical field
The present invention relates to a kind of distiller, be specially adapted to the distillation of brandy, belong to distiller technical field of structures.
Background technology
Brandy is a kind of beverage wine forming through distillation, existing brandy distillation equipment is Charente kettle formula distiller, this distiller is mainly comprised of boiler, preheater and condenser etc., complex structure, use inconvenience, need carry out twice distillation and just can make more than 60% original brandy of alcoholic strength.
Summary of the invention
The object of the invention is to solve the weak point that above-mentioned prior art exists, a kind of reasonable in design is provided, easy to use, only carry out single flash and just can make the distiller of alcoholic strength 60% above original brandy.
The present invention is achieved through the following technical solutions:
Distiller, it is characterized in that comprising the first boiler 12 that first heater 14 is installed, the after-fractionating pot 33 of secondary heating mechanism 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, foreshot's condenser 25 for the low fume of condensation, four are connected by the pipeline of baiting valve is installed, the first boiler 12, on preheater 20, be separately installed with the first return channel 4, the second return channel 19, the first return channel 4, the second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return duct 21 communicating with after-fractionating pot 33 is installed in preheater 20, inlet valve 1 is installed on preheater 20, the below of foreshot's condenser 25 is provided with the condenser 28 for condensation height fume, on condenser 28, be provided with and survey drinking vessel 29 and water intaking valve 30,
Between described the first boiler 12 and preheater 20, by being installed, the pipeline of the first baiting valve 6 is connected, this pipeline is provided with the branch line being connected with after-fractionating pot 33, the second baiting valve 7 is installed on this branch line, between preheater 20 and foreshot's condenser 25, by the liquid back pipe of valve 27 is installed, is connected;
Described the first return channel 4 is connected with after-fractionating pot 33 by the first gooseneck 3 of the first valve 9 is installed, and the second return channel 19 is connected with foreshot's condenser 25 by the second gooseneck 17;
On described the first boiler 12, relief valve 8 is installed;
The outside of described foreshot's condenser 25 is provided with spilling water valve 22, and inside is provided with foreshot's condenser pipe 24, and visor 23 is installed on foreshot's condenser pipe 24;
Described the first boiler 12 is separately installed with the first blowoff valve 15, the second blowoff valve 16 with the bottom of after-fractionating pot 33;
On described the first return channel 4, the second return channel 19, condenser 28, thermometer is all installed;
The outer surface of described the first boiler 12 and after-fractionating pot 33 is separately installed with the first heat-insulation layer 13, the second heat-insulation layer 31;
Described the first boiler 12, after-fractionating pot 33, preheater 20 are separately installed with for showing the first liquid level tube 10, the second liquid level tube 11, the 3rd liquid level tube 2 of liquid level.
Distiller structural design of the present invention is reasonable in design, each parts are used in conjunction with, only carry out single flash and just can make the above original brandy of alcoholic strength 60%, save fuel, improve alcoholic efficiency, in addition, owing to adopting foreshot's condenser, make the original brandy that makes fine and smooth, be continuous, the alcohol that has promoted wine liquid is just spent.
Accompanying drawing explanation
Fig. 1: the structural representation of distiller of the present invention.
The specific embodiment
Below with reference to accompanying drawing, provide the specific embodiment of the present invention, be used for that the present invention is described further.
Embodiment 1
The distiller of the present embodiment, comprise the first boiler 12 that first heater 14 is installed, the after-fractionating pot 33 of secondary heating mechanism 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, foreshot's condenser 25 for the low fume of condensation, four are connected by the pipeline of baiting valve is installed, the first boiler 12, on preheater 20, be separately installed with the first return channel 4, the second return channel 19, the first return channel 4, the second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return duct 21 communicating with after-fractionating pot 33 is installed in preheater 20, inlet valve 1 is installed on preheater 20, the below of foreshot's condenser 25 is provided with the condenser 28 for condensation height fume, on condenser 28, be provided with and survey drinking vessel 29 and water intaking valve 30, between the first boiler 12 and preheater 20, by being installed, the pipeline of the first baiting valve 6 is connected, this pipeline is provided with the branch line being connected with after-fractionating pot 33, the second baiting valve 7 is installed on this branch line, between preheater 20 and foreshot's condenser 25, by the liquid back pipe of valve 27 is installed, is connected, the first return channel 4 is connected with after-fractionating pot 33 by the first gooseneck 3 of the first valve 9 is installed, and the second return channel 19 is connected with foreshot's condenser 25 by the second gooseneck 17, on the first boiler 12, relief valve 8 is installed, the outside of foreshot's condenser 25 is provided with flowing water valve 22, and inside is provided with foreshot's condenser pipe 24, and visor 23 is installed on foreshot's condenser pipe 24, the first boiler 12 is separately installed with the first blowoff valve 15, the second blowoff valve 16 with the bottom of after-fractionating pot 33,
On the first return channel 4, the second return channel 19, condenser 28, thermometer is all installed; The outer surface of the first boiler 12 and after-fractionating pot 33 is separately installed with the first heat-insulation layer 13, the second heat-insulation layer 31;
The first boiler 12, after-fractionating pot 33, preheater 20 are separately installed with for showing the first liquid level tube 10, the second liquid level tube 11, the 3rd liquid level tube 2 of liquid level.
Alcoholic principle: first by relief valve 8, the first baiting valve 6, the second baiting valve 7 is opened, zymotic fluid injects preheater 20 through inlet valve 1, add to the first boiler 12, 75% of after-fractionating pot 33 capacity, then close relief valve 8 and the first baiting valve 6, the second baiting valve 7, to after the zymotic fluid of preheater 20 injection 75% capacity, close inlet valve 1 again, open the first valve 9, primary heater 14 and secondary heater 32 are connected, the first thermometer 5 and the second thermometer 18 are looked in sight, when temperature reaches 85 degrees Celsius, water intaking valve 30 and spilling water valve 22 are opened, the temperature of controlling the 3rd thermometer 26 is no more than 40 degrees Celsius, close the secondary heater 32 of after-fractionating pot 33, the wine vapour of the first boiler 12 continues to be heated to out wine vapour by the zymotic fluid in after-fractionating pot 33, wine vapour slowly heats the zymotic fluid in preheater 20 through the wine vapour return duct 21 of preheater 20 inside, wine vapour continues through the second gooseneck 17, enter foreshot's condenser 25, low wine vapour easily liquefies is had foreshot's condenser pipe 24 of cold water to be condensed into wine liquid by inside, remain in foreshot's condenser 25 inside, height quality liquor vapour is entered inside and is had by tube connector in the spiral copper pipe in the condenser 28 of cold water, through condensation, form wine liquid and enter survey drinking vessel 29, again the access of wine liquid is contained to drinking vessel, when the first thermometer 5 reaches 100 degrees Celsius, open secondary heater 32, close primary heater 14 simultaneously, after-fractionating pot 33 continues distillation, at this moment open relief valve 8, the raffinate of the first boiler 12 inside is discharged by the second blowoff valve 16, by valve 27, the wine liquid in foreshot's condenser 25 and the interior preheated zymotic fluid of preheater 20 are injected in the first boiler 12 again, again preheater 20 is injected to a certain amount of zymotic fluid, close secondary heater 32, open primary heater 14 simultaneously and continue distillation, circulation is constantly distilled to zymotic fluid and uses up according to this, for the last time the zymotic fluid in preheater 20 is injected in after-fractionating pot 33 until distill complete, open the first blowoff valve 15, the second blowoff valve 16 and relief valve 8 drain raffinate.
Distiller structural design of the present invention is reasonable in design, each parts are used in conjunction with, only carry out single flash and just can make the above original brandy of alcoholic strength 60%, save fuel, improve alcoholic efficiency, in addition, owing to adopting foreshot's condenser, make the original brandy that makes fine and smooth, be continuous, the alcohol that has promoted wine liquid is just spent.
Claims (6)
1. distiller, it is characterized in that comprising the first boiler (12) that first heater (14) is installed, the after-fractionating pot (33) of secondary heating mechanism (32) is installed, be installed on the preheater (20) of after-fractionating pot (33) top, foreshot's condenser (25) for the low fume of condensation, four are connected by the pipeline of baiting valve is installed, the first boiler (12), on preheater (20), be separately installed with the first return channel (4), the second return channel (19), the first return channel (4), the second return channel (19) is respectively by pipeline and after-fractionating pot (33), foreshot's condenser (25) is connected, the fume return duct (21) communicating with after-fractionating pot (33) is installed in preheater (20), inlet valve (1) is installed on preheater (20), the below of foreshot's condenser (25) is provided with the condenser (28) for condensation height fume, on condenser (28), be provided with and survey drinking vessel (29) and water intaking valve (30),
Between described the first boiler (12) and preheater (20), by being installed, the pipeline of the first baiting valve (6) is connected, this pipeline is provided with the branch line being connected with after-fractionating pot (33), the second baiting valve (7) is installed on this branch line, between preheater (20) and foreshot's condenser (25), by the liquid back pipe of valve (27) is installed, is connected;
Relief valve (8) is installed on described the first boiler (12);
The outside of described foreshot's condenser (25) is provided with spilling water valve (22), and inside is provided with foreshot's condenser pipe (24), and visor (23) is installed on foreshot's condenser pipe (24).
2. according to distiller claimed in claim 1, it is characterized in that described the first return channel (4) is connected with after-fractionating pot (33) by first gooseneck (3) of the first valve (9) is installed, the second return channel (19) is connected with foreshot's condenser (25) by the second gooseneck (17).
3. according to distiller claimed in claim 1, it is characterized in that described the first boiler (12) and the bottom of after-fractionating pot (33) are separately installed with the first blowoff valve (15), the second blowoff valve (16).
4. according to distiller claimed in claim 1, it is characterized in that described the first return channel (4), the second return channel (19), condenser are all provided with thermometer on (28).
5. according to distiller claimed in claim 1, it is characterized in that the outer surface of described the first boiler (12) and after-fractionating pot (33) is separately installed with the first heat-insulation layer (13), the second heat-insulation layer (31).
6. according to distiller claimed in claim 1, it is characterized in that described the first boiler (12), after-fractionating pot (33), preheater (20) are separately installed with the first liquid level tube (10), the second liquid level tube (11), the 3rd liquid level tube (2) for showing liquid level.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310154554.2A CN103194364B (en) | 2013-04-28 | 2013-04-28 | Distiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310154554.2A CN103194364B (en) | 2013-04-28 | 2013-04-28 | Distiller |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103194364A CN103194364A (en) | 2013-07-10 |
| CN103194364B true CN103194364B (en) | 2014-08-27 |
Family
ID=48717184
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310154554.2A Expired - Fee Related CN103194364B (en) | 2013-04-28 | 2013-04-28 | Distiller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103194364B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105132270A (en) * | 2015-10-13 | 2015-12-09 | 张新军 | Distilling system and method of distilled liquor |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103992930A (en) * | 2014-05-03 | 2014-08-20 | 张家口奥斯特不锈钢工程有限公司 | Novel efficient energy-saving wine distillation equipment |
| GB2552297B (en) | 2016-06-15 | 2020-01-08 | Russell Distillers Ltd | Liquid treatment apparatus, distillation apparatus, and method of distillation |
| CN107012058B (en) * | 2017-05-19 | 2023-05-19 | 贵州省仁怀市茅台镇郑氏酒业有限公司 | Pressurized wine steaming device |
| CN107574103B (en) * | 2017-09-06 | 2023-10-20 | 温州大宇科技有限公司 | Double-kettle distillation equipment with wine mixing function |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU932826A1 (en) * | 1980-03-05 | 1984-04-07 | Всесоюзный Ордена Трудового Красного Знамени Научно-Исследовательский Институт Виноделия И Виноградства "Магарач" | Method and apparatus for preparing brandy alcohol |
| FR2552567A1 (en) * | 1983-09-23 | 1985-03-29 | Prulho Robert Sa | Alcoholometry control device for an installation processing spirits, especially by distillation, and installation comprising it. |
| CN2408121Y (en) * | 2000-01-07 | 2000-11-29 | 无锡轻工大学 | Kettle type distillation device for producing multiple brandy wines |
| CN1318638A (en) * | 2000-04-14 | 2001-10-24 | 山东泰山生力源集团股份有限公司 | Fruit wine distilling equipment and technology |
| CN2481723Y (en) * | 2001-06-20 | 2002-03-13 | 北京华企爱普酒业技术开发有限公司 | Fruit liquor fermentation liquid pot type distilling device |
| CN201275426Y (en) * | 2008-10-08 | 2009-07-22 | 薛万杰 | Retorts |
| CN203174076U (en) * | 2013-04-28 | 2013-09-04 | 刘霞 | Distiller |
-
2013
- 2013-04-28 CN CN201310154554.2A patent/CN103194364B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU932826A1 (en) * | 1980-03-05 | 1984-04-07 | Всесоюзный Ордена Трудового Красного Знамени Научно-Исследовательский Институт Виноделия И Виноградства "Магарач" | Method and apparatus for preparing brandy alcohol |
| FR2552567A1 (en) * | 1983-09-23 | 1985-03-29 | Prulho Robert Sa | Alcoholometry control device for an installation processing spirits, especially by distillation, and installation comprising it. |
| CN2408121Y (en) * | 2000-01-07 | 2000-11-29 | 无锡轻工大学 | Kettle type distillation device for producing multiple brandy wines |
| CN1318638A (en) * | 2000-04-14 | 2001-10-24 | 山东泰山生力源集团股份有限公司 | Fruit wine distilling equipment and technology |
| CN2481723Y (en) * | 2001-06-20 | 2002-03-13 | 北京华企爱普酒业技术开发有限公司 | Fruit liquor fermentation liquid pot type distilling device |
| CN201275426Y (en) * | 2008-10-08 | 2009-07-22 | 薛万杰 | Retorts |
| CN203174076U (en) * | 2013-04-28 | 2013-09-04 | 刘霞 | Distiller |
Non-Patent Citations (1)
| Title |
|---|
| 李佩，等.连续生产白兰地酒精的水平蒸发装置.《酿酒科技》.1980,(第3期),第32-33页. * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105132270A (en) * | 2015-10-13 | 2015-12-09 | 张新军 | Distilling system and method of distilled liquor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103194364A (en) | 2013-07-10 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20140827 |