CN104818198A - Strong liquor distillation device - Google Patents
Strong liquor distillation device Download PDFInfo
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- CN104818198A CN104818198A CN201510208075.3A CN201510208075A CN104818198A CN 104818198 A CN104818198 A CN 104818198A CN 201510208075 A CN201510208075 A CN 201510208075A CN 104818198 A CN104818198 A CN 104818198A
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- distillation
- storage tank
- condenser
- valve
- pipeline
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
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- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a strong liquor distillation device, comprising a feeding heating tank, a distillation unit, a condenser, and a liquor discharging device. The distillation unit comprises a first distillation unit and a second distillation unit, an alcohol evaporating opening is arranged at the upper end of the feeding heating tank, the alcohol evaporating opening is provided with a distillation cap hollowed from top to bottom, an upper outlet of the distillation cap is in pipeline connection with a first three-way valve, and a second communicating port of the first three-way valve and a feed inlet of a first distillation column are in pipeline connection. An outlet of a first dephlegmator is connected with a second three-way valve in a pipeline mode, a second communicating port of the second three-way valve and a feed inlet of a second distillation column are in pipeline connection, an outlet of a second dephlegmator is connected with a feed inlet of the condenser, the first and the second distillation columns are both formed by splicing distillation trays of the same number in the vertical direction, and the first and the second distillation columns are arranged side by side in equal height. The strong liquor distillation device has the advantage of reasonable layout of overall height.
Description
Technical field
The present invention relates to a kind of distillation plant of earthquake intensity wine.
Background technology
The earthquake intensity wine such as vodka with cereal or potato for raw material, need through distilling the alcohol made up to 95 degree, desalinate to 40 degree to 60 degree with distilled water again, and through activated carbon filtration, make vinosity more sparkling and crystal-clear clear, colourless and light tasty and refreshing, make people feel sweetless, not bitter, not puckery, only have the stimulation as roaring flame, form the characteristic that vodka is original in style.Owing to needing the alcohol made up to 95 degree, the mutual split of distillation tower tray that all needs much save just can reach, and causes the height of equipment very high, for the height-limited system in general spirits factory building room.Therefore, be necessary to carry out improvement and design to the distillation plant of earthquake intensity wine.
Summary of the invention
The object of the invention is the shortcoming and defect existed to overcome prior art, and the distillation plant of the earthquake intensity wine providing a kind of whole height rationally distributed.
For achieving the above object, technical scheme of the present invention includes the heating tank that feeds intake, distillation unit, condenser and Wine discharging apapratus, described distillation unit includes the first distillation unit and after-fractionating unit, the first described distillation unit comprises the first distillation column and is arranged at the first partial condenser above the first distillation column, described after-fractionating unit comprises after-fractionating post and is arranged at the second partial condenser above after-fractionating post, the vaporized alcohol mouth that the upper end of the described heating tank that feeds intake is provided with, this vaporized alcohol mouth is provided with the still pot cap be communicated with up and down, the upper end discharge port upper pipeline of this still pot cap is connected with the first T-valve, second connected entrance of this first T-valve is connected with the opening for feed pipeline of the first distillation column, the discharge port upper pipeline of the first described partial condenser is connected with the second T-valve, second connected entrance of this second T-valve is connected with the opening for feed pipeline of after-fractionating post, the described discharge port of the second partial condenser is connected with the opening for feed of condenser, the first described distillation column is spliced up and down with the distillation tower tray of after-fractionating post by identical joint number, and this first distillation column and after-fractionating post contour layout side by side.
Further setting is that the third connecting mouth of described the first T-valve is connected with the opening for feed of condenser by main line, and the third connecting mouth dish of the second described T-valve is connected on this main line.
Further setting is that the bottom of described the first distillation column, after-fractionating post and condenser is respectively arranged with the first storage tank, the second storage tank and the 3rd storage tank, this first storage tank, the second storage tank and the mutual pipeline connection of the 3rd storage tank, and the cooling water outlet of the first described partial condenser is connected with the first storage tank phase pipeline, the cooling water outlet of the second described partial condenser is connected with the second storage tank phase pipeline.
Further setting be the often joint distillation tower tray of the first described distillation column and after-fractionating post sidewall on dish be connected to the backflow branch road of backflow to the heating tank that feeds intake, and each backflow branch road is provided with backflow branch road control valve.
Further setting is that the upper end docking that described alcohol steam exports is provided with still pot cap, this still pot cap includes lower joint flange, shape guide shell with a tight waist and spherical diffusion cylinder from top to bottom successively, described shape guide shell with a tight waist include circumferential hoop around arc barrel, position in the axis positively biased being centrally located at arc barrel of the arc wheel profile of the vertical section of this arc barrel.By the still pot cap of this setting, when can prevent from distilling, " flutterring pot " phenomenon occurs, and it makes the steam of overhead product have partial reflux in the annular diffusion barrel position of still pot cap, thus define slight refinery distillation, particularly crucially, position in the axis positively biased being centrally located at arc barrel of the arc wheel profile of the vertical section of this arc barrel, when distilling, opposing steam flow effect can be drastically increased, greatly improve rectification effect.
Advantage of the present invention is by distillation column step-by-step design, and the first distillation column and after-fractionating post contour layout side by side, reduce height, the design of three storage tanks, can make water coolant recycle, and reduces floor space.
Below in conjunction with specification drawings and specific embodiments, the present invention is described further.
Accompanying drawing explanation
Fig. 1 specific embodiment of the invention structural representation.
Embodiment
Below by embodiment, the present invention is specifically described, is only used to further illustrate the present invention, can not limiting the scope of the present invention be interpreted as.
The specific embodiment of the present invention as shown in Figure 1, include the heating tank 1 that feeds intake, distillation unit 2, condenser 3 and Wine discharging apapratus 4, described distillation unit 2 includes the first distillation unit 21 and after-fractionating unit 22, the first partial condenser 212 that the first described distillation unit 21 comprises the first distillation column 211 and is arranged at above the first distillation column, the second partial condenser 222 that described after-fractionating unit 22 comprises after-fractionating post 221 and is arranged at above after-fractionating post 221, the vaporized alcohol mouth 11 that the described upper end feeding intake heating tank 1 is provided with, this vaporized alcohol mouth 11 is provided with the still pot cap 5 be communicated with up and down, this still pot cap 5 includes lower joint flange 51 from top to bottom successively, shape guide shell 52 with a tight waist and spherical diffusion cylinder 53, described shape guide shell 52 with a tight waist include circumferential hoop around arc barrel, position in axis 5212 positively biased that the center 5211 of the arc wheel profile 521 of the vertical section of this arc barrel is positioned at arc barrel.
The upper end discharge port upper pipeline of this still pot cap 5 of the present embodiment is connected with the first T-valve 61, second connected entrance 612 of this first T-valve 61 is connected with opening for feed 2111 pipeline of the first distillation column 211, discharge port 2121 upper pipeline of the first described partial condenser 212 is connected with the second T-valve 62, second connected entrance 622 of this second T-valve 62 is connected with opening for feed 2211 pipeline of after-fractionating post 221, the described discharge port 2221 of the second partial condenser 222 is connected with the opening for feed 31 of condenser 3, the first described distillation column 211 is spliced up and down with the distillation tower tray a of after-fractionating post 221 by identical joint number, and this first distillation column 211 and after-fractionating post 221 contour layout side by side.
In addition, the third connecting mouth 613 of the first T-valve 61 described in the present embodiment is connected by the opening for feed of main line 71 with condenser 3, and third connecting mouth 623 dish of the second described T-valve 62 is connected on this main line 71.
In addition, the first distillation column 211 described in the present embodiment, the bottom of after-fractionating post 221 and condenser 3 is respectively arranged with the first storage tank 81, second storage tank 82 and the 3rd storage tank 83, this first storage tank 81, second storage tank 82 and the 3rd storage tank 83 pipeline connection mutually, and the cooling water outlet 2122 of the first described partial condenser 212 is connected with the first storage tank 81 phase pipeline, the cooling water outlet 2222 of the second described partial condenser 222 is connected with the second storage tank 82 phase pipeline, on the sidewall of the often joint distillation tower tray a of the first described distillation column 211 and after-fractionating post 221, dish is connected to the backflow branch road 72 of backflow to the heating tank that feeds intake, and each backflow branch road is provided with backflow branch road control valve 721.
Claims (5)
1. the distillation plant of an earthquake intensity wine, include the heating tank that feeds intake, distillation unit, condenser and Wine discharging apapratus, it is characterized in that: described distillation unit includes the first distillation unit and after-fractionating unit, the first described distillation unit comprises the first distillation column and is arranged at the first partial condenser above the first distillation column, described after-fractionating unit comprises after-fractionating post and is arranged at the second partial condenser above after-fractionating post, the vaporized alcohol mouth that the upper end of the described heating tank that feeds intake is provided with, this vaporized alcohol mouth is provided with the still pot cap be communicated with up and down, the upper end discharge port upper pipeline of this still pot cap is connected with the first T-valve, second connected entrance of this first T-valve is connected with the opening for feed pipeline of the first distillation column, the discharge port upper pipeline of the first described partial condenser is connected with the second T-valve, second connected entrance of this second T-valve is connected with the opening for feed pipeline of after-fractionating post, the described discharge port of the second partial condenser is connected with the opening for feed of condenser, the first described distillation column is spliced up and down with the distillation tower tray of after-fractionating post by identical joint number, and this first distillation column and after-fractionating post contour layout side by side.
2. the distillation plant of a kind of earthquake intensity wine according to claim 1, is characterized in that: the third connecting mouth of the first described T-valve is connected with the opening for feed of condenser by main line, the third connecting mouth dish of the second described T-valve is connected on this main line.
3. the distillation plant of a kind of earthquake intensity wine according to claim 1, it is characterized in that: the bottom of the first described distillation column, after-fractionating post and condenser is respectively arranged with the first storage tank, the second storage tank and the 3rd storage tank, this first storage tank, the second storage tank and the mutual pipeline connection of the 3rd storage tank, and the cooling water outlet of the first described partial condenser is connected with the first storage tank phase pipeline, the cooling water outlet of the second described partial condenser is connected with the second storage tank phase pipeline.
4. the distillation plant of a kind of earthquake intensity wine according to claim 1, it is characterized in that: on the sidewall of the often joint distillation tower tray of the first described distillation column and after-fractionating post, dish is connected to the backflow branch road of backflow to the heating tank that feeds intake, and each backflow branch road is provided with backflow branch road control valve.
5. the distillation plant of a kind of earthquake intensity wine according to claim 1, it is characterized in that: described still pot cap includes lower joint flange, shape guide shell with a tight waist and spherical diffusion cylinder from top to bottom successively, described shape guide shell with a tight waist include circumferential hoop around arc barrel, position in the axis positively biased being centrally located at arc barrel of the arc wheel profile of the vertical section of this arc barrel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510208075.3A CN104818198B (en) | 2015-04-28 | 2015-04-28 | Strong liquor distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510208075.3A CN104818198B (en) | 2015-04-28 | 2015-04-28 | Strong liquor distillation device |
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| Publication Number | Publication Date |
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| CN104818198A true CN104818198A (en) | 2015-08-05 |
| CN104818198B CN104818198B (en) | 2017-01-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510208075.3A Active CN104818198B (en) | 2015-04-28 | 2015-04-28 | Strong liquor distillation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113198195A (en) * | 2021-04-27 | 2021-08-03 | 浏阳高朗烈酒酿造有限公司 | Wine liquid distillation device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN203653529U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Three-time distiller |
| CN203653530U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Secondary distiller |
| CN203653528U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Brandy tower type distiller |
| CN204589145U (en) * | 2015-04-28 | 2015-08-26 | 温州大宇科技有限公司 | A kind of distillation plant of earthquake intensity wine |
-
2015
- 2015-04-28 CN CN201510208075.3A patent/CN104818198B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN203653529U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Three-time distiller |
| CN203653530U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Secondary distiller |
| CN203653528U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Brandy tower type distiller |
| CN204589145U (en) * | 2015-04-28 | 2015-08-26 | 温州大宇科技有限公司 | A kind of distillation plant of earthquake intensity wine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113198195A (en) * | 2021-04-27 | 2021-08-03 | 浏阳高朗烈酒酿造有限公司 | Wine liquid distillation device |
| CN113198195B (en) * | 2021-04-27 | 2024-05-07 | 浏阳高朗烈酒酿造有限公司 | Wine liquid distillation device |
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| Publication number | Publication date |
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| CN104818198B (en) | 2017-01-25 |
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Denomination of invention: Strong liquor distillation device Effective date of registration: 20191224 Granted publication date: 20170125 Pledgee: Industrial Bank Co., Ltd. Wenzhou Branch Pledgor: Wenzhou Science and Technology Ltd. of Daewoo Registration number: Y2019330000376 |