CN104818198B - Strong liquor distillation device - Google Patents
Strong liquor distillation device Download PDFInfo
- Publication number
- CN104818198B CN104818198B CN201510208075.3A CN201510208075A CN104818198B CN 104818198 B CN104818198 B CN 104818198B CN 201510208075 A CN201510208075 A CN 201510208075A CN 104818198 B CN104818198 B CN 104818198B
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- CN
- China
- Prior art keywords
- distillation
- condenser
- storage tank
- way valve
- distillation column
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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
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 equipment of earthquake intensity wine.
Background technology
The earthquake intensity wine such as Little water., with corn or Rhizoma Solani tuber osi as raw material, needs to make up to 95 degree of ethanol through distillation,
Desalinated to 40 degree to 60 degree with distilled water again, and filter through activated carbon, make vinosity more sparkling and crystal-clear clear, colourless and light refreshing
Mouthful, make one to feel sweetless, not bitter, not puckery, stimulation only as roaring flame, form the original in style characteristic of Little water..Due to needing
Make up to 95 degree of ethanol, the mutual split of distillation tower tray of a lot of sections in need can be only achieved, lead to the height of equipment
Very high, the height-limited system for general spirits Factory Building room.Therefore, it is necessary to improvement and design is carried out to the distillation equipment of earthquake intensity wine.
Content of the invention
The invention aims to overcoming the shortcoming and defect that prior art exists, and provide a kind of whole height layout
The distillation equipment of rational earthquake intensity wine.
For achieving the above object, the technical scheme is that and include the heating tank that feeds intake, distillation unit, condenser and go out
Drinking vessel, described distillation unit includes the first distillation unit and after-fractionating unit, and the first described distillation unit includes
One distillation column and be arranged at the first fractional condenser above the first distillation column, described after-fractionating unit include after-fractionating post and
It is arranged at the second fractional condenser above after-fractionating post, the vaporized alcohol mouth that the upper end of the described heating tank that feeds intake is provided with, should
The boiler cap connecting up and down is provided with vaporized alcohol mouth, the upper end discharging opening upper pipeline of this boiler cap is connected with the one or three
Port valve, the second connected entrance of this first three-way valve is connected with the charging aperture pipeline of the first distillation column, described the first fractional condenser
Discharging opening upper pipeline is connected with the second three-way valve, the second connected entrance of this second three-way valve and the charging aperture pipeline of after-fractionating post
It is connected, the described discharging opening of the second fractional condenser is connected with the charging aperture of condenser, the first described distillation column and after-fractionating
Post is spliced up and down by the distillation tower tray of identical joint number, and this first distillation column and after-fractionating post contour arrangement side by side.
Setting is the charging aperture phase by main line and condenser for the third connecting mouth of the first described three-way valve further
Even, the third connecting mouth disk of the second described three-way valve is connected on this main line.
Setting is that the bottom of described the first distillation column, after-fractionating post and condenser is respectively arranged with the first storage further
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 described first
The coolant outlet of fractional condenser is connected with the first storage tank phase pipeline, the described coolant outlet of the second fractional condenser and the second storage tank
Phase pipeline connects.
Setting is that on the first described distillation column and the side wall of often section distillation tower tray of after-fractionating post, disk is connected to further
It is provided with backflow branch road control valve on the backflow branch road flowing back to the heating tank that feeds intake, and each backflow branch road.
Setting is that the upper end docking of described alcohol steam outlet is provided with boiler cap further, this boiler cap under
Include lower adpting flange, shape guide shell with a tight waist and spherical diffusion cylinder to upper successively, described shape guide shell with a tight waist includes week
To the arc barrel of cincture, the arc wheel profile of the longitudinal section of this arc barrel is centrally located at the axis positively biased of arc barrel
Upper position.The boiler cap being arranged by this, can prevent phenomenon of " flutterring pot " during distillation from occurring, and it makes the steam of distillation exist
There is partial reflux the annular diffusion barrel position of boiler cap, thus defining slight rectifying action, particularly critical, this arc
The arc wheel profile of the longitudinal section of shape barrel is centrally located at position in the axis positively biased of arc barrel, in distillation, can pole
The earth improves opposing steam flow effect, greatly improves rectification effect.
It is an advantage of the invention that by distillation column segment design, and the first distillation column and after-fractionating post contour arrangement side by side,
Reduce height, the design of three storage tanks, cooling water can be made to be recycled, reduce floor space.
With reference to specification drawings and specific embodiments, the present invention is described further.
Brief description
Fig. 1 specific embodiment of the invention structural representation.
Specific embodiment
Below by embodiment, the present invention is specifically described, is served only for the present invention is further described, no
It is understood that as limiting the scope of the present invention.
The specific embodiment of the present invention as shown in Figure 1, includes 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, and the first described distillation is single
Unit 21 includes the first distillation column 211 and is arranged at the first fractional condenser 212 above the first distillation column, described after-fractionating unit
22 the second fractional condensers 222 including after-fractionating post 221 and being arranged at after-fractionating post 221 top, the described heating tank 1 that feeds intake
The vaporized alcohol mouth 11 that is provided with of upper end, this vaporized alcohol mouth 11 is provided with the boiler cap 5 connecting up and down, this boiler
Cap 5 includes lower adpting flange 51, shape guide shell 52 with a tight waist and spherical diffusion cylinder 53 from top to bottom successively, and described shape with a tight waist is led
Flow cartridge 52 include circumferentially around arc barrel, 5211, the center of the arc wheel profile 521 of the longitudinal section of this arc barrel
Position in axis 5212 positively biased of arc barrel.
The upper end discharging opening upper pipeline of this boiler cap 5 of the present embodiment is connected with the first three-way valve 61, this first three-way valve
61 the second connected entrance 612 is connected with charging aperture 2111 pipeline of the first distillation column 211, the going out of described the first fractional condenser 212
Material mouth 2121 upper pipeline is connected with the second three-way valve 62, the second connected entrance 622 of this second three-way valve 62 and after-fractionating post 221
Charging aperture 2211 pipeline be connected, the described discharging opening 2221 of the second fractional condenser 222 is connected with the charging aperture 31 of condenser 3,
The first described distillation column 211 is spliced by the distillation tower tray a of identical joint number up and down with after-fractionating post 221, and this
One distillation column 211 and after-fractionating post 221 contour arrangement side by side.
In addition, the third connecting mouth 613 of the first three-way valve 61 described in the present embodiment passes through main line 71 and condenser 3
Charging aperture is connected, and third connecting mouth 623 disk of the second described three-way valve 62 is connected on this main line 71.
Additionally, the bottom of the first distillation column 211, after-fractionating post 221 and condenser 3 described in the present embodiment is respectively provided with
There are the first storage tank 81, the second storage tank 82 and the 3rd storage tank 83, this first storage tank 81, the second storage tank 82 and the 3rd storage tank 83 are mutually managed
Road connects, and the described coolant outlet 2122 of the first fractional condenser 212 is connected with the first storage tank 81 phase pipeline, and described second
The coolant outlet 2222 of fractional condenser 222 is connected with the second storage tank 82 phase pipeline, the first described distillation column 211 and after-fractionating
On the side wall of often section distillation tower tray a of post 221, disk is connected to the backflow branch road 72 flowing back to the heating tank that feeds intake, and each branch road that flows back
On be provided with backflow branch road control valve 721.
Claims (1)
1. a kind of distillation equipment of earthquake intensity wine, includes the heating tank that feeds intake, distillation unit, condenser and Wine discharging apapratus, its feature exists
In: described distillation unit includes the first distillation unit and after-fractionating unit, and the first described distillation unit includes first
Distillation column and the first fractional condenser being arranged above the first distillation column, described after-fractionating unit includes after-fractionating post and sets
It is placed in the second fractional 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 wine
It is provided with, on essence evaporation mouth, the boiler cap connecting up and down, the upper end discharging opening upper pipeline of this boiler cap is connected with the first threeway
Valve, the second connected entrance of this first three-way valve is connected with the charging aperture pipeline of the first distillation column, the going out of described the first fractional condenser
Material mouth upper pipeline is connected with the second three-way valve, the charging aperture pipeline phase of the second connected entrance of this second three-way valve and after-fractionating post
Even, the described discharging opening of the second fractional condenser is connected with the charging aperture of condenser, the first described distillation column and after-fractionating post
Distillation tower tray by identical joint number is spliced up and down, and this first distillation column and after-fractionating post contour arrangement side by side, institute
The third connecting mouth of the first three-way valve stated is connected with the charging aperture of condenser by main line, and the of described the second three-way valve
Tee joint mouth disk is connected on this main line, and the bottom of described the first distillation column, after-fractionating post and condenser is respectively arranged with
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 described
The coolant outlet of the first fractional condenser be connected with the first storage tank phase pipeline, the described coolant outlet of the second fractional condenser and
Two storage tank phase pipelines connect, and on the side wall of often section distillation tower tray of the first described distillation column and after-fractionating post, disk is connected to backflow
To the backflow branch road of the heating tank that feeds intake, and each backflow branch road on be provided with backflow branch road control valve, described boiler cap from
Under include lower adpting flange, shape guide shell with a tight waist and spherical diffusion cylinder successively to upper, described shape guide shell with a tight waist includes
Circumferentially around arc barrel, the arc wheel profile of the longitudinal section of this arc barrel is just being centrally located at the axis of arc barrel
Position on the upper side.
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 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104818198A CN104818198A (en) | 2015-08-05 |
| CN104818198B true CN104818198B (en) | 2017-01-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510208075.3A Active CN104818198B (en) | 2015-04-28 | 2015-04-28 | Strong liquor distillation device |
Country Status (1)
| Country | Link |
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| CN (1) | CN104818198B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113198195B (en) * | 2021-04-27 | 2024-05-07 | 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 |
| 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 |
| CN203653530U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Secondary distiller |
| CN203653529U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Three-time 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 |
| 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 |
| CN203653530U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Secondary distiller |
| CN203653529U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Three-time 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104818198A (en) | 2015-08-05 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| EXSB | Decision made by sipo to initiate substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
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 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |