CN206318971U - Grape wine fractionating device - Google Patents
Grape wine fractionating device Download PDFInfo
- Publication number
- CN206318971U CN206318971U CN201621474326.9U CN201621474326U CN206318971U CN 206318971 U CN206318971 U CN 206318971U CN 201621474326 U CN201621474326 U CN 201621474326U CN 206318971 U CN206318971 U CN 206318971U
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- CN
- China
- Prior art keywords
- heat exchanger
- fractionating column
- fractionating
- grape wine
- pipeline
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- Expired - Fee Related
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The application is related to a kind of grape wine distilling apparatus, more particularly to a kind of grape wine fractionating device；It includes boiler, heat exchanger, fractionating column and condenser；Boiler is connected by pipeline with heat exchanger, and heat exchanger is connected by pipeline with fractionating column；It is characterized in that：Fractionation column base, which is provided with, to be provided with the waste pipe of first switch valve and is provided with the fractionating column of second switch valve.Due to implementing above-mentioned technical proposal, the application ensures that the vapours that boiler is produced is not contacted directly with grape wine Normal juice by heat exchanger, improves grape wine quality；By the design of waste pipe and fractionating column fractionating column can be made followed by carry out fractionation process having performed distillation technique, obtain high alcohol concentration（50%vol to 95%vol）Height fractionation wine former wine and low alcohol concentration（5%vol to 0%vol）Low fractionation wine former wine, the two obtained carry out allotment and the anhydrous allotment of grape wine can be achieved, and raw material is naturally safe, and obtained grape wine mouthfeel is natural, best in quality.
Description
Technical field
The application is related to a kind of grape wine distilling apparatus, more particularly to a kind of grape wine fractionating device.
Background technology
At present in tower grape wine distilling apparatus, high temperature and high pressure steam, steam direct heating grape wine are produced by boiler
Normal juice, gas is become by active ingredients such as the aroma-producing substance in grape wine Normal juice, ethanol, recycles condensing unit by the part gas
Body condensation gets off to be formed distillation former wine in fluid preservation.There is following drawback in this technology；Distillation former wine needs to enter using distilled water
Row allotment, the quality of water differs, and causes final grape wine quality level uneven, such as adds the bad water of quality and even there is safety
Hidden danger；It is 15%vol to 40%vol to distill the general alcohol concentration after distillation of former wine, and tower grape wine distilling apparatus is in distillation
Remaining liquid contains substantial amounts of alcoholic content after process, and this part abandons as waste material and extremely wasted.
The content of the invention
The purpose of the application is the grape for proposing a kind of saving water resource, being sufficiently separated alcohol, improving grape wine quality
Wine fractionating device.
What the application was realized in：Grape wine fractionating device, it includes boiler, heat exchanger, fractionating column and condenser；Pot
Stove is connected by pipeline with heat exchanger, and heat exchanger is connected by pipeline with fractionating column；It is characterized in that：Fractionation column base is provided with peace
Waste pipe and the fractionating column for being provided with second switch valve equipped with first switch valve；Steam (vapor) outlet, steam are provided with the top of fractionating column
Outlet is connected by pipeline with condenser overhead；Fractionating column top is provided with inlet, and inlet is by being provided with the 3rd switch valve
It is connected with the pipeline of the first hydraulic pump with condenser bottom；Condenser bottom is additionally provided with the collecting pipe equipped with the 4th switch valve.
Further, waste pipe and fractionating column are located at the sustained height position of fractionation column base.
Further, the pipeline between heat exchanger and fractionating column is two-way setting, wherein flowing to the pipe of heat exchanger from fractionating column
Road is provided with down-comer, and down-comer is connected to heat exchanger.
Further, the bottom of heat exchanger is provided with return duct, and return tank is connected to thermal storage device, heat accumulation by the second hydraulic pump
Device is connected with the water inlet end of boiler.
Further, the installation site of waste pipe and fractionating column is below the pipeline for being used to be connected with heat exchanger on fractionating column
Installation site.
Due to implementing above-mentioned technical proposal, the application ensures that the vapours that boiler is produced is former not with grape wine by heat exchanger
Juice is directly contacted, and improves grape wine quality；By the design of waste pipe and fractionating column fractionating column can be made to perform distillation technique
Fractionation process is followed by carried out, high alcohol concentration is obtained（50%vol to 95%vol）Height fractionation wine former wine and low alcohol concentration
（5%vol to 0%vol）Low fractionation wine former wine, the two obtained carry out allotment and the anhydrous allotment of grape wine, raw material day can be achieved
So safe, obtained grape wine mouthfeel is natural, best in quality.
Brief description of the drawings
The concrete structure of the application is provided by following drawings and Examples：
Fig. 1 is the structural representation of the application most preferred embodiment.
Legend：1. boiler, 2. heat exchangers, 3. fractionating columns, 4. condensers, 5. first switch valves, 6. waste pipes, 7. second open
Pass valve, 8. fractionating columns, 9. steam (vapor) outlets, 10. inlets, 11. the 3rd switch valves, 12. first hydraulic pumps, 13. the 4th switch valves,
14. collecting pipe, 15. down-comers, 16. return ducts, 17. second hydraulic pumps.
Embodiment
The application is not limited by following embodiments, can be determined according to the technical scheme of the application with actual conditions specific
Embodiment.
As shown in figure 1, grape wine fractionating device includes boiler 1, heat exchanger 2, fractionating column 3 and condenser 4；Boiler 1 passes through
Pipeline is connected with heat exchanger 2, and heat exchanger 2 is connected by pipeline with fractionating column 3；It is characterized in that：The bottom of fractionating column 3 is provided with installation
There is the waste pipe 6 of first switch valve 5 and the fractionating column 8 of second switch valve 7 is installed；The top of fractionating column 3 is provided with steam (vapor) outlet 9,
Steam (vapor) outlet 9 is connected by pipeline with the top of condenser 4；The top of fractionating column 3 is provided with inlet 10, and inlet 10 is by being provided with
The pipeline of 3rd switch valve 11 and the first hydraulic pump 12 is connected with the bottom of condenser 4；The bottom of condenser 4 is additionally provided with opens equipped with the 4th
Close the collecting pipe 14 of valve 13.
When carrying out distillation technique, first switch valve 5 is opened, second switch valve 7, the 3rd switch valve 11 and the 4th is closed and opens
Close valve 13；Utilize the heat exchange function in heat exchanger 2, it is to avoid Boiler Steam pollutes grape wine Normal juice, improve grape wine quality；When
Distillation technique terminates, and 15%vol to 40%vol distillation former wine is collected in condenser 4 by steam (vapor) outlet 9, will remain in point
The waste material containing a large amount of magazines evaporated in tower 3 is discharged by waste pipe 6；When carrying out fractionation process, first switch valve 5 is closed,
Second switch valve 7 is opened, the 3rd switch valve 11 is opened, the 4th switch valve 13 is closed；Distillation former wine in condenser 4 is in the first liquid
Reentered in the presence of press pump 12 by inlet 10 and fractionation processing, high alcohol concentration are carried out in fractionating column 3（50%vol is extremely
95%vol）Height fractionation wine former wine enter drainer in vapour form and reclaim, low alcohol concentration（5%vol to 0%vol）It is low
Degree fractionation wine former wine can also first pass through the discharge collection of fractionating column 8 in liquid form, and the two obtained is allocated, with natural low
Degree fractionation wine former wine replaces the distilled water for being used for allocating in the prior art, and the anhydrous allotment of grape wine, different proportion mixing can be achieved
The grape wine that alcohol concentration is 2%vol to 90%vol, raw materials used natural safety, the grape wine mouthfeel finally given is made in proportioning
It is natural, best in quality；The application structure of modification is simple, and effect is obvious.Heat exchanger 2 is existing public technology, is by hot-fluid
Equipment of the heat by heat transfer to cold flow, while ensureing that hot and cold stream does not cross.
Fractionation process in the application actually refers to that single flash wine former wine is repeatedly distilled in fractionating column 3, because
When the boiling point of material is sufficiently close to, about to differ 20 degree, 20%vol being can only obtain to 35%vol's using the common way of distillation
Single flash wine former wine, is difficult to be kept completely separate alcohol and water；And fractionating process can make single flash wine former wine in fractionating column 3 from tower
Bottom is passed through to tower top repeatedly distills repeatedly, final high alcohol concentration（50%vol to 95%vol）Height be fractionated wine former wine with steam
Form is reclaimed into drainer, low alcohol concentration（5%vol to 0%vol）Low fractionation wine former wine can also stay in liquid form
The bottom of towe of fractionating column 3；When in the ideal situation, alcohol fully evaporates, the remaining liq alcohol concentration stayed in fractionating column 3 is 0%
Vol, now obtains grape water；Almost Perfect is completely separated alcohol and water.
As shown in figure 1, waste pipe 6 and fractionating column 8 are located at the sustained height position of the bottom of fractionating column 3.
As shown in figure 1, the pipeline between heat exchanger 2 and fractionating column 3 is two-way setting, wherein flowing to heat exchanger 2 from fractionating column 3
Pipeline be provided with down-comer 15, down-comer 15 is connected to heat exchanger 2.Thermal cycle can be so carried out, heat energy is made full use of, it is ensured that steamed
Evaporate, fractionation process it is thorough.
As shown in figure 1, the bottom of heat exchanger 2 is provided with return duct 16, return tank is connected to heat accumulation by the second hydraulic pump 17
Device, thermal storage device is connected with the water inlet end of boiler 1.It need not be so continuously the after softening water of boiler 1, need to only be filled up first
Softened water, saves water source；The water for entering thermal storage device additionally by the second hydraulic pump 17 can save coal between 70-90 degree,
Improve the efficiency of boiler 1.
As shown in figure 1, the installation site of waste pipe 6 and fractionating column 8 is below being used to be connected with heat exchanger 2 on fractionating column 3
Pipeline installation site.
Above technical characteristic constitutes the most preferred embodiment of the application, and it has stronger adaptability and optimal implementation effect
Really, inessential technical characteristic can be increased and decreased according to actual needs, the need for meeting different situations.
Claims (8)
1. a kind of grape wine fractionating device, including boiler, heat exchanger, fractionating column and condenser；Boiler passes through pipeline and heat exchanger
It is connected, heat exchanger is connected by pipeline with fractionating column；It is characterized in that：Fractionation column base is provided with the row for being provided with first switch valve
Useless pipe and the fractionating column for being provided with second switch valve；Steam (vapor) outlet is provided with the top of fractionating column, steam (vapor) outlet passes through pipeline and condensation
It is connected at the top of device；Fractionating column top is provided with inlet, and inlet is by being provided with the pipeline of the 3rd switch valve and the first hydraulic pump
It is connected with condenser bottom；Condenser bottom is additionally provided with the collecting pipe equipped with the 4th switch valve.
2. grape wine fractionating device according to claim 1, it is characterised in that：Waste pipe and fractionating column are located at Fractionator Bottom
The sustained height position in portion.
3. grape wine fractionating device according to claim 1 or 2, it is characterised in that：Pipeline between heat exchanger and fractionating column
For two-way setting, wherein the pipeline for flowing to heat exchanger from fractionating column is provided with down-comer, down-comer is connected to heat exchanger.
4. grape wine fractionating device according to claim 1 or 2, it is characterised in that：The bottom of heat exchanger is provided with return duct,
Return tank is connected to thermal storage device by the second hydraulic pump, and thermal storage device is connected with the water inlet end of boiler.
5. grape wine fractionating device according to claim 3, it is characterised in that：The bottom of heat exchanger is provided with return duct, returns
Stream tank is connected to thermal storage device by the second hydraulic pump, and thermal storage device is connected with the water inlet end of boiler.
6. the grape wine fractionating device according to claim 1 or 2 or 5, it is characterised in that：The installation of waste pipe and fractionating column
Position is below on fractionating column for the installation site for the pipeline being connected with heat exchanger.
7. grape wine fractionating device according to claim 3, it is characterised in that：The installation site of waste pipe and fractionating column is equal
Less than the installation site for the pipeline for being used to be connected with heat exchanger on fractionating column.
8. grape wine fractionating device according to claim 4, it is characterised in that：The installation site of waste pipe and fractionating column is equal
Less than the installation site for the pipeline for being used to be connected with heat exchanger on fractionating column.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621474326.9U CN206318971U (en) | 2016-12-30 | 2016-12-30 | Grape wine fractionating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621474326.9U CN206318971U (en) | 2016-12-30 | 2016-12-30 | Grape wine fractionating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206318971U true CN206318971U (en) | 2017-07-11 |
Family
ID=59261190
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621474326.9U Expired - Fee Related CN206318971U (en) | 2016-12-30 | 2016-12-30 | Grape wine fractionating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206318971U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108949397A (en) * | 2018-09-12 | 2018-12-07 | 新疆红河农业科技有限公司 | A kind of efficient destilling tower |
| CN113234567A (en) * | 2021-04-08 | 2021-08-10 | 陕西聚能新创煤化科技有限公司 | System and process for preparing wine by stripping and distilling by using carrier gas method |
-
2016
- 2016-12-30 CN CN201621474326.9U patent/CN206318971U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108949397A (en) * | 2018-09-12 | 2018-12-07 | 新疆红河农业科技有限公司 | A kind of efficient destilling tower |
| CN108949397B (en) * | 2018-09-12 | 2023-10-27 | 新疆红河农业科技有限公司 | High-efficiency distillation tower |
| CN113234567A (en) * | 2021-04-08 | 2021-08-10 | 陕西聚能新创煤化科技有限公司 | System and process for preparing wine by stripping and distilling by using carrier gas method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170711 Termination date: 20171230 |