CN205974481U - Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy - Google Patents
Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy Download PDFInfo
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- CN205974481U CN205974481U CN201620682465.4U CN201620682465U CN205974481U CN 205974481 U CN205974481 U CN 205974481U CN 201620682465 U CN201620682465 U CN 201620682465U CN 205974481 U CN205974481 U CN 205974481U
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Abstract
The utility model provides a carry heating device centering medicine liqueur to carry solution after the low pressure wine vapour that produces mixes in high -pressure wine vapour that wine liquid heating evaporation system of cyclic utilization wine vapour heat energy, this system produced in with wine vapour generator and the evaporative concentration ware and heat, consumption that this kind of wine liquid heating evaporation system can effectual reduction steam, improve equipment's the thermal efficiency reduces the condensation energy consumption of condenser, and the processing that does not increase follow -up alcohol rectifying column is simultaneously loaded.
Description
Technical field
This utility model is related to a kind of wine liquid heating evaporation system recycling wine vapour heat energy.
Background technology
Chinese medicine wine dipper concentration of liquid medicine evaporation equipment most at present is typically all directly to be passed through water vapour to heater to enter
Row heating, alcohol steam produced by heating process can all after condenser is condensed into wine liquid through rectification and purification again by
Use, due to being that whole alcohol steams are all condensed using condenser, the high energy consumption of condenser, and the consumption of water vapour also ten
Divide big, the material channel of heater also usually coking can because the temperature of water vapour is high, even results in showing of blocking
As.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of energy consumption low, and heater thing
Material passage is difficult the wine liquid heating evaporation system of coking.
In order to achieve the above object, this utility model employs the following technical solutions：
A kind of wine liquid heating evaporation system recycling wine vapour heat energy, including wine vapour generator, steam jet ejector,
Evaporation concentrator and heater, the upper end of described evaporation concentrator is provided with low pressure wine vapour venthole, on described wine vapour generator
It is provided with steam inlet and high pressure wine vapour venthole, described steam inlet is connected with jet chimney, and described high pressure wine vapour goes out vapour
Mouth is connected with the air intake of described steam jet ejector by gas pipeline, and the venthole of described steam jet ejector passes through
Mixing wine steam pipe road is connected with described heater, and the wine dipper that described heater is used for heating in described evaporation concentrator is molten
Liquid, and the low pressure wine vapour of generation is delivered in evaporation concentrator described low pressure wine vapour venthole passes through circulating line and described steaming
The air intake connection of vapour jet ejector.
Preferably, described gas pipeline is provided with wine steam control valve, and described wine steam control valve is used for controlling high pressure wine vapour to enter
Enter the flow of described steam jet ejector, thus controlling mixed wine stripping temperature.
Further, also include wine liquid and reclaim subsystem, described wine liquid is reclaimed subsystem and includes being connected successively by recovery channel
Logical thin drinking vessel, row's wine valve and receive fat, the wine inlet of described thin drinking vessel is connected with the wine outlet of described heater, wine vapour warp
The wine liquid being formed after crossing heat exchange, wine liquid is recovered by this system, thus reaching the purpose recycling.
Further, also include wine liquid and supplement subsystem, described wine liquid supplement subsystem include by wine liquid supplement pipeline according to
The replenishment valve of secondary connection, booster pump and heat exchanger, described heat exchanger is provided with wine outlet and water inlet, on described wine vapour generator
It is provided with wine inlet and outlet, described wine outlet is connected with described wine inlet, and described water inlet is connected with described outlet, works as wine
When vapour generator requires supplementation with wine liquid, replenishment valve is opened, and row's wine valve cuts out, and starts booster pump simultaneously and wine liquid injection wine vapour occurs
In device.
Further, because the low pressure wine vapour that steam jet ejector reclaims is that have a certain proportion of, unnecessary low pressure wine vapour
Can be reclaimed by wine vapour condensation subsystem, described wine vapour condensation subsystem is connected on described circulating line, and it includes
Vacuum breaker, condenser, vacuum pump and separator, described vacuum breaker, condenser and separator pass through condensation pipe according to
Secondary connection, described vacuum pump is connected with described separator, and the wine outlet of separator is connected with described receipts fat, and described vacuum pump makes
Wine vapour passes sequentially through vacuum breaker, condenser and separator, and low pressure wine vapour is converted into wine liquid after wine vapour condensation subsystem,
Flow into and receive fat.
Preferably, described jet chimney is provided with steam control valve, and described steam control valve is used for controlling wine vapour generator
Interior wine steam raising speed, thus indirectly adjust the air pressure size in wine vapour generator.
Preferably, described high pressure wine vapour venthole is arranged on the top of described wine vapour generator, and described low pressure wine vapour goes out vapour
Mouth is arranged on the top of described evaporation concentrator, and because high pressure wine vapour and low pressure wine vapour all can gather upwards, therefore venthole sets
Put in the discharge that can more contribute to wine vapour above container and minimizing wine vapour and carry liquid.
Preferably, described heater is arranged on the inner side of described evaporation concentrator, or, described heater is located at institute
State the outside of evaporation concentrator, the wine inlet of heater is connected with the bottom of described evaporation concentrator, described heater
Venthole is connected with the top of described evaporation concentrator.
Compared with prior art, this utility model innovative do not use water vapour directly Chinese medicinal liquor carried with solution carry out
Heating, but by way of mixing the low pressure wine vapour in the high pressure wine vapour in wine vapour generator and recovery concentrator, to heating
Device carries out heat supply, by this heat-supplying mode, is effectively reduced the consumption of water vapour, improves the thermal efficiency of equipment, subtract
Lack the condensation energy consumption of condenser, do not increase the process load of follow-up ethanol refinery tower simultaneously.
Brief description
Fig. 1 is a kind of structural representation of embodiment of the present utility model；
Fig. 2 is the structural representation of another embodiment of the present utility model.
Specific embodiment
Embodiment one：
A kind of wine liquid heating evaporation system recycling wine vapour heat energy providing referring to Fig. 1 to Fig. 2, the present invention, including
Wine vapour generator 1, steam jet ejector 2, evaporation concentrator 3 and heater 4, the upper end of described evaporation concentrator 3 is provided with
Low pressure wine vapour venthole 31, the side of evaporation concentrator 3 is provided with the charging aperture 32 for supplementing wine dipper solution, and described wine vapour occurs
Device 1 is provided with steam inlet 11 and high pressure wine vapour venthole 12, and described steam inlet 11 is connected with jet chimney 10, described
High pressure wine vapour venthole 12 is connected with the air intake 21 of described steam jet ejector 2 by gas pipeline 13, described steam spray
The venthole 22 penetrating compressor 2 is connected with described heater 4 by mixing wine steam pipe road 23, and described heater 4 is used for adding
Wine dipper solution in the described evaporation concentrator 3 of heat, and the low pressure wine vapour of generation is delivered to described low pressure wine in evaporation concentrator 3
Vapour venthole 31 is connected with the air intake 21 of described steam jet ejector 2 by circulating line 33.
It should be noted that heater 4 can be provided in inner side or the outside of evaporation concentrator 3, when heater 4
When being arranged on evaporation concentrator 3 inner side, it can be simple heat exchanger, by the wine dipper solution heating boiling in evaporation concentrator 3
Rise；And when heater 4 is arranged on evaporation concentrator 3 outside, this heater needs to be set to split pipe heater (figure
Not shown), the wine inlet of this heater is connected with the bottom of described evaporation concentrator 3, the described venthole splitting pipe heater with
The top connection of described evaporation concentrator 3.
Embodiment two：
The present embodiment place different from embodiment one is, is additionally provided with 2 subsystems, and specific embodiment is：
Above-mentioned wine liquid heating evaporation system is additionally provided with wine liquid and reclaims subsystem 5, and described wine liquid reclaims subsystem 5 and includes
Thin drinking vessel 51, row's wine valve 52 and receipts fat 54, the wine inlet of described thin drinking vessel 51 and the institute being sequentially communicated by recovery channel 53
State the wine outlet connection of heater 4, the wine liquid that wine vapour is formed after heat exchange, wine liquid is recovered by this system, thus side
Just next time reuses.
Furthermore it is also possible to set up the wine for supplementing wine liquid to wine vapour generator 1 on the basis of reclaiming subsystem 5
Liquid supplements subsystem 6, and described wine liquid supplements subsystem 6 and includes supplementing, by wine liquid, replenishment valve 61, the increasing that pipeline 63 is sequentially communicated
Press pump 62 and heat exchanger 64, described heat exchanger 64 is provided with wine outlet 641 and water inlet 642, and described wine vapour generator 1 is provided with
Wine inlet 14 and outlet 15, described wine outlet 641 is connected with described wine inlet 14, described water inlet 642 and described outlet
15 connections.When wine vapour generator 1 requires supplementation with wine liquid, replenishment valve 61 is opened, and row's wine valve 52 cuts out, and starts booster pump 62 simultaneously
Wine liquid is injected in wine vapour generator 1.
As a kind of preferred scheme, due to the low pressure wine vapour that steam jet ejector 2 reclaims be have a certain proportion of, many
Remaining low pressure wine vapour can be reclaimed by wine vapour condensation subsystem 7, and described wine vapour condensation subsystem 7 is connected to described circulation
On pipeline 33, it includes vacuum breaker 71, condenser 72, vacuum pump 73 and separator 74, described vacuum breaker 71, condensation
Device 72 and separator 74 are sequentially communicated by condensation pipe 75, and described vacuum pump 73 is connected with described separator 74, separator 74
Wine outlet 741 with described receipts fat 54 connect, described vacuum pump 73 makes wine vapour pass sequentially through vacuum breaker 71, condenser 72
With separator 74, final low pressure wine vapour conversion formation wine liquid, flow into and receive fat 54.
As a kind of preferred scheme, above-mentioned gas pipeline 13 is provided with wine steam control valve 16, described wine steam control valve 16
For controlling high pressure wine vapour to enter the flow of described steam jet ejector 2, thus controlling mixed wine stripping temperature；And it is above-mentioned
Jet chimney 10 be provided with steam control valve 101, described steam control valve 101 is used for controlling wine vapour in wine vapour generator 1
Evaporation rate, thus indirectly adjust the air pressure size in wine vapour generator 1.
As a kind of preferred scheme, described high pressure wine vapour venthole 12 is arranged on the top of described wine vapour generator 1, institute
State the top that low pressure wine vapour venthole 31 is arranged on described evaporation concentrator 3, because high pressure wine vapour and low pressure wine vapour all can be upwards
Accumulation, therefore venthole be arranged on container top can more contribute to wine vapour discharge and reduce wine vapour in carry liquid.
The announcement of book and teaching according to the above description, this utility model those skilled in the art can also be to above-mentioned reality
The mode of applying is changed and is changed.Therefore, this utility model is not limited to specific embodiment disclosed and described above, right
Some modifications and changes of the present utility model should also be as falling in scope of the claims of the present utility model.Additionally, to the greatest extent
Employ some specific terms in pipe this specification, but these terms are merely for convenience of description, not to this utility model
Constitute any restriction.
Claims (8)
1. a kind of wine liquid heating evaporation system recycling wine vapour heat energy it is characterised in that：Including wine vapour generator, steam spray
Penetrate compressor, evaporation concentrator and heater, the upper end of described evaporation concentrator is provided with low pressure wine vapour venthole, described wine vapour
Generator is provided with steam inlet and high pressure wine vapour venthole, and described steam inlet is connected with jet chimney, described high pressure
Wine vapour venthole is connected with the air intake of described steam jet ejector by gas pipeline, the going out of described steam jet ejector
Steam ports is passed through mixing wine steam pipe road and is connected with described heater, and described heater is used for heating in described evaporation concentrator
Wine dipper solution, and the low pressure wine vapour of generation is delivered in evaporation concentrator, described low pressure wine vapour venthole passes through circulating line
Connect with the air intake of described steam jet ejector.
2. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 1 it is characterised in that：Institute
State gas pipeline and be provided with wine steam control valve, described wine steam control valve is used for controlling high pressure wine vapour to enter described steam jet compression
The flow of device.
3. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 1 it is characterised in that：Also
Reclaim subsystem including wine liquid, described wine liquid reclaims thin drinking vessel, the row's wine valve that subsystem includes being sequentially communicated by recovery channel
With receive fat, the wine inlet of described thin drinking vessel connected with the wine outlet of described heater.
4. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 3 it is characterised in that：Also
Supplement subsystem including wine liquid, described wine liquid supplements subsystem and includes supplementing, by wine liquid, replenishment valve, the increasing that pipeline is sequentially communicated
Press pump and heat exchanger, described heat exchanger is provided with wine outlet and water inlet, and described wine vapour generator is provided with wine inlet and water outlet
Mouthful, described wine outlet is connected with described wine inlet, and described water inlet is connected with described outlet.
5. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 3 it is characterised in that：Also
Including wine vapour condensation subsystem, described wine vapour condensation subsystem is connected on described circulating line, and it includes vacuum breaker, cold
Condenser, vacuum pump and separator, described vacuum breaker, condenser and separator are sequentially communicated by condensation pipe, described true
Empty pump is connected with described separator, and the wine outlet of separator is connected with described receipts fat, and described vacuum pump makes wine vapour pass sequentially through
Vacuum breaker, condenser and separator.
6. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 1 it is characterised in that：Institute
State jet chimney and be provided with steam control valve, described steam control valve is used for controlling the wine steam raising speed in wine vapour generator.
7. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 1 it is characterised in that：Institute
State the top that high pressure wine vapour venthole is arranged on described wine vapour generator, it is dense that described low pressure wine vapour venthole is arranged on described evaporation
The top of contracting device.
8. a kind of wine liquid heating evaporation system recycling wine vapour heat energy according to claim 1 it is characterised in that：Institute
State the inner side that heater is arranged on described evaporation concentrator, or, described heater is located at the outer of described evaporation concentrator
Side, the wine inlet of heater is connected with the bottom of described evaporation concentrator, the venthole of described heater and described evaporation
The top connection of concentrator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620682465.4U CN205974481U (en) | 2016-06-29 | 2016-06-29 | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620682465.4U CN205974481U (en) | 2016-06-29 | 2016-06-29 | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974481U true CN205974481U (en) | 2017-02-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620682465.4U Active CN205974481U (en) | 2016-06-29 | 2016-06-29 | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107299040A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | Multistage distillation brewing device |
| CN107299039A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | The manufacture method of multistage distillation Brewing equipment |
| CN107937228A (en) * | 2018-01-11 | 2018-04-20 | 维度绿色科技（广州）有限公司 | A kind of steam regeneration device using Spirit vapour thermal energy |
-
2016
- 2016-06-29 CN CN201620682465.4U patent/CN205974481U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107299040A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | Multistage distillation brewing device |
| CN107299039A (en) * | 2017-08-25 | 2017-10-27 | 遵义市永宏金属设备有限公司 | The manufacture method of multistage distillation Brewing equipment |
| CN107937228A (en) * | 2018-01-11 | 2018-04-20 | 维度绿色科技（广州）有限公司 | A kind of steam regeneration device using Spirit vapour thermal energy |
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| GR01 | Patent grant |