CN103194364A - Distiller - Google Patents
Distiller Download PDFInfo
- Publication number
- CN103194364A CN103194364A CN2013101545542A CN201310154554A CN103194364A CN 103194364 A CN103194364 A CN 103194364A CN 2013101545542 A CN2013101545542 A CN 2013101545542A CN 201310154554 A CN201310154554 A CN 201310154554A CN 103194364 A CN103194364 A CN 103194364A
- Authority
- CN
- China
- Prior art keywords
- pot
- condenser
- preheater
- foreshot
- 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.)
- Granted
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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000003517 fume Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims description 29
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 230000035622 drinking Effects 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 6
- 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 4
- 230000001476 alcoholic effect Effects 0.000 description 4
- 239000000446 fuel Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- 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 the distiller technical field of structures.
Background technology
[0002] brandy is a kind of through distilling the wine of drinking that forms, existing brandy distillation plant is Charente kettle formula distiller, this distiller mainly is made up of still pot, preheater and condenser etc., complex structure, use inconvenience, need carry out twice distillation and just can make the original brandy of alcoholic strength more than 60%.
Summary of the invention
The objective 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 the distiller that single flash just can make alcoholic strength 60% above original brandy.
The present invention is achieved through the following technical solutions:
Distiller, it is characterized in that comprising first still pot 12 that first heating unit 14 is installed, the after-fractionating pot 33 of second heating unit 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, the foreshot's condenser 25 that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot 12, be separately installed with first return channel 4 on the preheater 20, second return channel 19, first return channel 4, second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return line 21 that communicates with after-fractionating pot 33 is installed in the preheater 20, feed valve 1 is installed on the preheater 20, the below of foreshot's condenser 25 is equipped with the condenser 28 for condensation height fume, is equipped with on the condenser 28 to survey drinking vessel 29 and water intaking valve 30;
Be connected by the pipeline that first baiting valve 6 is installed between described first still pot 12 and the preheater 20, this pipeline is provided with the branch line that is connected with after-fractionating pot 33, second baiting valve 7 is installed on this branch line, is connected by the liquid returning tube that valve 27 is installed between preheater 20 and the foreshot's condenser 25;
Described first return channel 4 is connected with after-fractionating pot 33 by first swan neck 3 that first valve 9 is installed, and second return channel 19 is connected with foreshot's condenser 25 by second swan neck 17;
On described first still pot 12 pressure release valve 8 is installed;
The outside of described foreshot's condenser 25 is equipped with spilling water valve 22, and inside is equipped with foreshot's prolong 24, and visor 23 is installed on foreshot's prolong 24;
Described first still pot 12 is separately installed with first wash water valve 15, second wash water valve 16 with the bottom of after-fractionating pot 33;
On described first return channel 4, second return channel 19, the condenser 28 thermometer is installed all;
The outside surface of described first still pot 12 and after-fractionating pot 33 is separately installed with first thermal insulation layer 13, second thermal insulation layer 31;
Described first still pot 12, after-fractionating pot 33, preheater 20 are separately installed with for first liquid level tube 10, second liquid level tube 11, the 3rd liquid level tube 2 that show liquid level.
Distiller structure design of the present invention is reasonable in design, each parts is used, only carry out single flash and just can make alcoholic strength 60% above original brandy, fuel economy, improve wine efficient processed, in addition, owing to adopt foreshot's condenser, make the original brandy exquisiteness that makes, be continuous, the alcohol that has promoted wine liquid is just spent.
Description of drawings
Fig. 1: the structural representation of distiller of the present invention.
Embodiment
Provide the specific embodiment of the present invention below with reference to accompanying drawing, be used for that the present invention is described further.
Embodiment 1
The distiller of present embodiment, comprise first still pot 12 that first heating unit 14 is installed, the after-fractionating pot 33 of second heating unit 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, the foreshot's condenser 25 that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot 12, be separately installed with first return channel 4 on the preheater 20, second return channel 19, first return channel 4, second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return line 21 that communicates with after-fractionating pot 33 is installed in the preheater 20, feed valve 1 is installed on the preheater 20, the below of foreshot's condenser 25 is equipped with the condenser 28 for condensation height fume, is equipped with on the condenser 28 to survey drinking vessel 29 and water intaking valve 30; Be connected by the pipeline that first baiting valve 6 is installed between first still pot 12 and the preheater 20, this pipeline is provided with the branch line that is connected with after-fractionating pot 33, second baiting valve 7 is installed on this branch line, is connected by the liquid returning tube that valve 27 is installed between preheater 20 and the foreshot's condenser 25; First return channel 4 is connected with after-fractionating pot 33 by first swan neck 3 that first valve 9 is installed, and second return channel 19 is connected with foreshot's condenser 25 by second swan neck 17; On first still pot 12 pressure release valve 8 is installed; The outside of foreshot's condenser 25 is equipped with flowing water valve 22, and inside is equipped with foreshot's prolong 24, and visor 23 is installed on foreshot's prolong 24; First still pot 12 is separately installed with first wash water valve 15, second wash water valve 16 with the bottom of after-fractionating pot 33;
On first return channel 4, second return channel 19, the condenser 28 thermometer is installed all; The outside surface of first still pot 12 and after-fractionating pot 33 is separately installed with first thermal insulation layer 13, second thermal insulation layer 31;
First still pot 12, after-fractionating pot 33, preheater 20 are separately installed with for first liquid level tube 10, second liquid level tube 11, the 3rd liquid level tube 2 that show liquid level.
Wine principle processed: at first with pressure release valve 8, first baiting valve 6, second baiting valve 7 is opened, fermented liquid injects preheater 20 through feed valve 1, add to first still pot 12,75% of after-fractionating pot 33 capacity, close pressure release valve 8 and first baiting valve 6 then, second baiting valve 7, close feed valve 1 after the fermented liquid with preheater 20 injections 75% capacity again, open first valve 9, primary heater 14 and secondary heater 32 are connected, first thermometer 5 and second thermometer 18 are looked in sight, when temperature reaches 85 degrees centigrade, 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 centigrade, close the secondary heater 32 of after-fractionating pot 33, the wine vapour of first still pot 12 continues to be heated to out wine vapour with the fermented liquid in the after-fractionating pot 33, wine vapour slowly heats the fermented liquid in the preheater 20 through the wine vapour return line 21 of preheater 20 inside, wine vapour continues through second swan neck 17, enter foreshot's condenser 25, low alcohol vapour liquefies is easily had foreshot's prolong 24 of cold water to be condensed into wine liquid by inside, remain in foreshot's condenser 25 inside, height quality liquor vapour enters inside and has by pipe connecting in the spiral copper pipe in the condenser 28 of cold water, form wine liquid through condensation and enter survey drinking vessel 29, again wine liquid is inserted and contain drinking vessel, when first thermometer 5 reaches 100 degrees centigrade, open secondary heater 32, close primary heater 14 simultaneously, after-fractionating pot 33 continues distillation, at this moment open pressure release valve 8, the raffinate of first still pot, 12 inside is discharged by second wash water valve 16, by valve 27 the good fermented liquid of preheating in the wine liquid in foreshot's condenser 25 and the preheater 20 is injected in first still pot 12 again, again preheater 20 is injected a certain amount of fermented liquid, close secondary heater 32, open primary heater 14 simultaneously and continue distillation, circulation constantly is distilled to fermented liquid and uses up according to this, with finishing until distillation in the injection of the fermented liquid in the preheater 20 after-fractionating pot 33, open first wash water valve 15 for the last time, second wash water valve 16 and pressure release valve 8 drain raffinate.
Distiller structure design of the present invention is reasonable in design, each parts is used, only carry out single flash and just can make alcoholic strength 60% above original brandy, fuel economy, improve wine efficient processed, in addition, owing to adopt foreshot's condenser, make the original brandy exquisiteness that makes, be continuous, the alcohol that has promoted wine liquid is just spent.
Claims (9)
1. distiller, it is characterized in that comprising first still pot (12) that first heating unit (14) is installed, the after-fractionating pot (33) of second heating unit (32) is installed, be installed on the preheater (20) of after-fractionating pot (33) top, the foreshot's condenser (25) that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot (12), be separately installed with first return channel (4) on the preheater (20), second return channel (19), first return channel (4), second return channel (19) is respectively by pipeline and after-fractionating pot (33), foreshot's condenser (25) is connected, the fume return line (21) that communicates with after-fractionating pot (33) is installed in the preheater (20), feed valve (1) is installed on the preheater (20), the below of foreshot's condenser (25) is equipped with the condenser (28) for condensation height fume, is equipped with on the condenser (28) to survey drinking vessel (29) and water intaking valve (30).
2. according to the described distiller of claim 1, it is characterized in that being connected by the pipeline that first baiting valve (6) is installed between described first still pot (12) and the preheater (20), this pipeline is provided with the branch line that is connected with after-fractionating pot (33), second baiting valve (7) is installed on this branch line, is connected by the liquid returning tube that valve (27) is installed between preheater (20) and the foreshot's condenser (25).
3. according to the described distiller of claim 1, it is characterized in that described first return channel (4) is connected with after-fractionating pot (33) by first swan neck (3) that first valve (9) is installed, second return channel (19) is connected with foreshot's condenser (25) by second swan neck (17).
4. according to the described distiller of claim 1, it is characterized in that being equipped with on described first still pot (12) pressure release valve (8).
5. according to the described distiller of claim 1, it is characterized in that the outside of described foreshot's condenser (25) is equipped with spilling water valve (22), inside is equipped with foreshot's prolong (24), and visor (23) is installed on foreshot's prolong (24).
6. according to the described distiller of claim 1, it is characterized in that described first still pot (12) and the bottom of after-fractionating pot (33) are separately installed with first wash water valve (15), second wash water valve (16).
7. according to the described distiller of claim 1, it is characterized in that described first return channel (4), second return channel (19), condenser all are equipped with thermometer on (28).
8. according to the described distiller of claim 1, it is characterized in that the outside surface of described first still pot (12) and after-fractionating pot (33) is separately installed with first thermal insulation layer (13), second thermal insulation layer (31).
9. according to the described distiller of claim 1, it is characterized in that described first still pot (12), after-fractionating pot (33), preheater (20) are separately installed with for first liquid level tube (10), second liquid level tube (11), the 3rd liquid level tube (2) that show 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 |
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CN103194364A true CN103194364A (en) | 2013-07-10 |
CN103194364B CN103194364B (en) | 2014-08-27 |
Family
ID=48717184
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201310154554.2A Expired - Fee Related CN103194364B (en) | 2013-04-28 | 2013-04-28 | Distiller |
Country Status (1)
Country | Link |
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CN (1) | CN103194364B (en) |
Cited By (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 |
CN107012058A (en) * | 2017-05-19 | 2017-08-04 | 贵州省仁怀市茅台镇郑氏酒业有限公司 | One kind pressurization wine-distilling device |
CN107574103A (en) * | 2017-09-06 | 2018-01-12 | 温州大宇科技有限公司 | Double kettle distillation equipments with rectification function |
CN109475785A (en) * | 2016-06-15 | 2019-03-15 | 拉塞尔制酒有限公司 | Distilling apparatus and its distillating method comprising the chamber for accommodating material to be extracted |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105132270B (en) * | 2015-10-13 | 2018-04-06 | 西藏农牧学院 | The Distallation systm and distillating method of Spirit |
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》 * |
Cited By (7)
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 |
CN109475785A (en) * | 2016-06-15 | 2019-03-15 | 拉塞尔制酒有限公司 | Distilling apparatus and its distillating method comprising the chamber for accommodating material to be extracted |
CN109475785B (en) * | 2016-06-15 | 2021-05-28 | 拉塞尔制酒有限公司 | Distillation device comprising a chamber for receiving a material to be extracted and method for distilling same |
US11278824B2 (en) | 2016-06-15 | 2022-03-22 | Russell Distillers Limited | Distillation apparatus comprising a chamber for holding material to be extracted and method thereof |
CN107012058A (en) * | 2017-05-19 | 2017-08-04 | 贵州省仁怀市茅台镇郑氏酒业有限公司 | One kind pressurization wine-distilling device |
CN107574103A (en) * | 2017-09-06 | 2018-01-12 | 温州大宇科技有限公司 | Double kettle distillation equipments with rectification function |
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 |
Also Published As
Publication number | Publication date |
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CN103194364B (en) | 2014-08-27 |
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Granted publication date: 20140827 |