CN107937228A - A kind of steam regeneration device using Spirit vapour thermal energy - Google Patents
A kind of steam regeneration device using Spirit vapour thermal energy Download PDFInfo
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- CN107937228A CN107937228A CN201810026786.2A CN201810026786A CN107937228A CN 107937228 A CN107937228 A CN 107937228A CN 201810026786 A CN201810026786 A CN 201810026786A CN 107937228 A CN107937228 A CN 107937228A
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- steam
- vapour
- switching path
- input terminal
- hot switching
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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 present invention is the steam regeneration device using Spirit vapour thermal energy, including vapour compression machine and heat exchanger, distillation equipment be equipped with steam inlet and wine vapor outlet；Vapour compression machine includes being used for the high steam input terminal, low-pressure steam input terminal and compression output terminal for connecting initial steam, and compression output terminal is connected with the steam inlet of distillation equipment；Heat exchanger is equipped with the first hot switching path and the second hot switching path that can carry out heat exchange, the wine vapor outlet of the input terminal connection distillation equipment of first hot switching path, the wine vapour that distillation equipment produces enters wine liquid collecting after the output terminal of the first hot switching path, the input terminal of second hot switching path is used to connect water supplement apparatus, the output terminal connection low-pressure steam input terminal of the second hot switching path.Compared with prior art, steam regeneration device of the invention reduces the cooling of wine vapour and steam-heated energy consumption using the thermal energy generation low-pressure steam of wine vapour, significantly reduces distillation cost by setting heat exchanger.
Description
Technical field
The invention belongs to white wine preparation field, and in particular to a kind of steam regeneration device using Spirit vapour thermal energy.
Background technology
Spirit brewing is needed to stir by dispensing, fermented, distills, and distillation is an important step in liquor production
Suddenly, need to consume substantial amounts of high steam in distillation process and material is heated, distill the wine vapour of gained in condensing unit
Finished product white wine is produced by condensing cooling.At present, liquor distilling apparatus generally cooling water the dialogue in a manner of heat exchange
The wine vapour of wine cools down, and it is converted into liquid by steam state so as to obtaining wine liquid, usually by conveyance conduit by wine vapour
It is introduced into condenser, cooling water directly carries out heat exchange with wine vapour by duct wall within the condenser, is recycled after forming wine liquid, and
The cooling used cooling water of wine vapour is directly discharged or discarded, and cooling water is increased to more than 50 degree by room temperature at this time, in this way,
The distillation process of white wine carries out, it is necessary to consume substantial amounts of cooling water without stoply, so that the significant wastage of water resource is caused,
Also, the heat of wine vapour cannot be recycled, it is unfavorable for energy saving.
Existing liquor distilling apparatus needs further improvement, and the distillation cost of white wine is reduced by reducing energy consumption, and
And lifting energy-saving effect.
The content of the invention
The goal of the invention of the present invention is to provide a kind of steam regeneration device using Spirit vapour thermal energy, by using steaming
The thermal energy generation low-pressure steam of wine vapour is evaporated, heating steam can be reduced and cool down the energy consumption of wine vapour and the distillation cost of white wine.
Steam regeneration device provided by the invention using Spirit vapour thermal energy includes vapour compression machine and heat exchanger, institute
Stating vapour compression machine includes being used for the high steam input terminal, low-pressure steam input terminal and compression output terminal for connecting initial steam, institute
Compression output terminal is stated to connect with the steam inlet of distillation equipment by the first steam conveying pipe；The heat exchanger is equipped with can be into
The first hot switching path and the second hot switching path of row heat exchange, the input terminal of first hot switching path pass through the first wine
The wine vapor outlet of vapour conveyance conduit and distillation equipment connects, output terminal of the wine vapour through the first hot switching path that distillation equipment produces
Enter wine liquid collecting afterwards, the input terminal of second hot switching path is used to connect water supplement apparatus, the second hot switching path
Output terminal connect the low-pressure steam input terminal；From distillation equipment output wine vapour by during the first hot switching path by second
Water heating evaporation in hot switching path forms low-pressure steam, and low-pressure steam is passed through distillation equipment after vapour compression machine pressurizes.
Compared with prior art, steam regeneration device of the invention, the thermal energy produced using Spirit vapour is in heat exchanger
Middle that water heating evaporation is generated low-pressure steam, low-pressure steam is compressed by vapour compression machine, and the regeneration produced after compression is steamed
Vapour returns to distillation equipment and reuses, and generates initial steam Recycling by recycling low pressure wine vapour thermal energy, effectively reduces distillation
Equipment water vapour consumes, and improves the thermal efficiency of equipment.The initial steam of the present invention, the heat source being primarily referred to as in evaporation operation are normal
Using fresh saturated steam, also referred to as raw steam.
Preferably, it is in parallel defeated equipped with initial steam between the high steam input terminal of the vapour compression machine and compression output terminal
Enter bypass, initial steam input bypass is equipped with bypass flow regulating valve, the initial steam input bypass and high steam input terminal
Between be equipped with power flow control valve；Steam-flow meter is installed, bypass flow regulating valve and dynamic on the first steam conveying pipe
Force flow adjustable valve corresponds to the quantity of steam of pipeline according to the feedback flow control of steam-flow meter.Steam-flow meter control, which enters, steams
The quantity of steam of equipment is evaporated, bypass flow regulating valve is opened when initial, the bypass flow tune when regenerated low-pressure steam gradually increases
Section valve gradually turns down, and the steam flow that steam-flow meter is flowed through after bypass flow regulating valve completely closes is flowed still above setting
During value, power steam regulating valve gradually turns down again, achievees the purpose that quantitative control with this.
Preferably, the heat exchanger include into vapour chamber, heat exchanging chamber and steam discharge chamber, the heat exchanging chamber be arranged on into vapour chamber with
Be equipped with some heat exchanger tubes between steam discharge chamber, in the heat exchanging chamber, the both ends of the heat exchanger tube be respectively communicated with described in into vapour chamber and row
Vapour chamber forms first hot switching path, and second hot switching path is arranged on the outside of heat exchanger tube；The steam discharge chamber is set
There is wine liquid outlet, wine liquid outlet is connected with wine liquid collecting.Wine vapour by heat exchanger tube when with the second hot switching path
Water mediate contact carry out heat exchange, the wine liquid of generation is discharged to wine liquid collecting from wine liquid outlet, and heat exchange and wine liquid are received
The mode of collection is simple, practical.
Preferably, the second hot switching path input terminal is equipped with the input terminal company of atomization box, water supplement apparatus and atomization box
Connect.Atomized water into by atomization box after water mist and be discharged into the second heat exchanger channels again and exchange heat with wine vapour, effectively improve low pressure steaming
The formation efficiency of vapour.
Preferably, the output terminal of second hot switching path passes through low-pressure steam recovery channel with low-pressure steam input terminal
Connection, low-pressure steam recovery channel are equipped with vapour liquid separator, and the input terminal of vapour liquid separator is defeated with the second hot switching path
Outlet connects, and the output terminal of vapour liquid separator is connected with low-pressure steam input terminal, the drain side of vapour liquid separator and water supplement apparatus
Connection.By setting vapour liquid separator to be separated low-pressure steam with unboiled water, ensure into the low of vapour compression machine
The vaporization of steam is pressed, improves the compression effect amount of regeneration steam, while make unboiled water be back in water supply tank again to make
With being conducive to energy saving.
Preferably, vacuum wind is equipped between the output terminal of the input terminal of the vapour liquid separator and the second hot switching path
Machine.The low-pressure steam in the second heat exchanger channels is quickly extracted out by vacuum blower, prevents low-pressure steam to be trapped in the second heat exchange
Occupied space in passage, to improve heat exchange efficiency, and improves the increment of the low-pressure steam of low-pressure steam recovery channel.
Preferably, the water supplement apparatus includes water supply tank, and water supply tank and the second hot switching path input terminal pass through filling pipe
Road connects, and water pipe connection is equipped with second heat exchanger；The steam discharge chamber is equipped with steam drain, and second heat exchanger is equipped with
The filling pipe input terminal and filling pipe output terminal being connected with water pipe, and the second heat exchange air intake and the second heat exchange row
Outlet, the second heat exchange air intake is connected with steam drain, in steam discharge chamber not liquefied wine vapour through second heat exchanger to filling pipe
In water preheated；The output terminal of second hot switching path passes through low-pressure steam recovery channel with low-pressure steam input terminal
Connection, low-pressure steam recovery channel are equipped with vapour liquid separator, and the input terminal of vapour liquid separator is defeated with the second hot switching path
Outlet connects, and the output terminal of vapour liquid separator is connected with low-pressure steam input terminal, the drain side of vapour liquid separator and water supplement apparatus
Connection.By setting the second heat exchanger to carry out secondary use to the heat of wine vapour, the cooling effectiveness of wine vapour is improved, in addition, passing through
The thermal energy of wine vapour carries out water the formation efficiency that preheating is conducive to improve low-pressure steam.By setting vapour liquid separator to steam low pressure
Vapour is separated with unboiled water, is ensured the vaporization into the low-pressure steam of vapour compression machine, is improved regeneration steam
Effect amount is compressed, while unboiled water is back in water supply tank and reuses, is conducive to energy saving.
Preferably, space of second hot switching path between heat exchanger tube and heat exchanging chamber, heat exchanging chamber are interior equipped with spiral
Shape deflector, helical form deflector outside heat exchange cavity wall connection, each heat exchanger tube are each passed through helical form deflector.Pass through setting
Deflector, makes water mist be flowed in the shape of a spiral by the water conservancy diversion of deflector, and is uniformly attached in heat exchange pipe outer wall and absorbs thermal energy, makes the
The heat exchanger effectiveness higher of one hot switching path and the second hot switching path.
Preferably, the drain side of the vapour liquid separator is provided with steam trap to prevent low-pressure steam is discharged to moisturizing from setting
It is standby, thin drinking vessel is installed to prevent uncooled wine vapour to be discharged to wine liquid collecting in the real wine liquid collecting.
Preferably, water supply tank outlet is equipped with high-pressure pump, and the high pressure pump outlet is connected with flowmeter, high-pressure pump according to
The feedback control rate of water make-up of flowmeter；The water supply tank is equipped with the inlet channel being connected with external water source, is installed on inlet channel
There is water compensating valve.System is realized automatic water supply by this setting, control water supply without artificial detection and water rate control is more accurate.
Brief description of the drawings
Fig. 1 is the principle of the present invention schematic diagram；
Fig. 2 is the structure diagram of heat exchanger；
Fig. 3 is a kind of principle sketch of preferred solution of the present invention.
Label declaration：
Distillation equipment 1, steam regeneration device 2, power flow control valve 201, bypass flow regulating valve 202, both vapor compression
Machine 203, steam-flow meter 204, heat exchanger 301, heat exchanging chamber 3011, into vapour chamber 3012, steam discharge chamber 3013, heat exchanger tube 3014,
Demarcation strip 3015, deflector 3016, steam (vapor) outlet 3017, water supply tank 302, atomization box 303, the heat of atomizer 3031, second are handed over
Parallel operation 304, vapour liquid separator 307, steam trap 309, vacuum blower 306, flowmeter 3023, water compensating valve 3022, dredge drinking vessel 305,
High-pressure pump 3021, check valve 308, the first steam conveying pipe 401, the first wine vapour conveyance conduit 501, wine liquid collecting 502,
Low-pressure steam recovery channel 402, moisturizing pipeline 601, inlet channel 602, water return pipeline 603, initial steam pipeline 403, initial steam
Input bypass 404.
Embodiment
Referring to Fig. 1-3, steam regeneration device 2 of the invention includes vapour compression machine 203 and heat exchanger 301, the steaming
Vapour compressor 203 includes being used for the high steam input terminal, low-pressure steam input terminal and compression output terminal for connecting initial steam, described
Compression output terminal is connected by the first steam conveying pipe 401 with the steam inlet of distillation equipment 1；The heat exchanger 301 is set
The first hot switching path and the second hot switching path of heat exchange can be carried out by having, and the input terminal of first hot switching path passes through
First wine vapour conveyance conduit 501 is connected with the wine vapor outlet of distillation equipment 1, and the wine vapour that distillation equipment 1 produces is through the first heat exchange
Entering wine liquid collecting 502 after the output terminal of passage, the input terminal of second hot switching path is used to connect water supplement apparatus,
The output terminal of second hot switching path connects the low-pressure steam input terminal；Pass through the first heat from the wine vapour that distillation equipment 1 exports
The water heating evaporation in the second hot switching path is formed into low-pressure steam during interchange channel, low-pressure steam is through vapour compression machine 203
Distillation equipment 1 is passed through after pressurization.
Compared with prior art, the steam regeneration device 2 of the invention using Spirit vapour thermal energy is by setting heat exchange
Device 301, using wine vapour thermal energy generation low-pressure steam with reduce wine vapour cooling and steam-heated energy consumption, by reduce energy consumption with
The distillation cost of white wine is reduced, there is preferable energy-saving effect.Since heat exchanger 301 is equipped be connected with water supplement apparatus second
Heat exchanger channels, the cooling water for being used in cooling wine vapour is heated generation low-pressure steam, effectively save to use water.
By taking the Distallation systm of the above-mentioned steam regeneration device 2 of application as an example, it includes distillation equipment 1,203 and of vapour compression machine
Heat exchanger 301, the distillation equipment 1 are equipped with steam inlet (not showing on figure) and wine vapor outlet (not showing on figure).The steam
Compressor 203 includes being used for the high steam input terminal, low-pressure steam input terminal and compression output terminal for connecting initial steam, the pressure
Contracting output terminal is connected by the first steam conveying pipe 401 with the steam inlet；The heat exchanger 301, which is equipped with, can carry out heat
The first hot switching path and the second hot switching path exchanged, the input terminal of first hot switching path are defeated by the first wine vapour
Pipeline 501 is sent to connect the wine vapor outlet, wine vapour enters wine liquid collecting 502 after the output terminal of the first hot switching path,
The input terminal of second hot switching path is used to connect water supplement apparatus, and the output terminal of the second hot switching path connects the low pressure
Steam input terminal；The wine vapour exported from distillation equipment 1 is by adding the water in the second hot switching path during the first hot switching path
Thermal evaporation forms low-pressure steam, and low-pressure steam is passed through distillation equipment 1 after the pressurization of vapour compression machine 203.Preferably, the high pressure
Steam input terminal connects exterior initial steam source by initial steam pipeline 403.
Workflow：Initial steam enters vapour compression machine 203 by high steam input terminal, and wine vapour is defeated by wine vapor outlet
The first hot switching path of heat exchanger 301 is sent to, the water supplement apparatus supplies water to the second hot switching path, and first heat is handed over
The fluid that changes in passage and the second hot switching path carries out heat exchange and produces wine liquid and low-pressure steam respectively, and the wine liquid of generation is through the
The output terminal of one heat exchanger channels is discharged and is recovered by wine liquid collection conduit；The low-pressure steam is through the second hot switching path
Output terminal is discharged to low-pressure steam input terminal, and the vapour compression machine 203 sucks low-pressure steam and initial steam and carries out compressed action,
First steam conveying pipe 401 is discharged to by the output terminal of the vapour compression machine 203 by the mixed vapour after compression work done,
And it is discharged to by steam inlet in distillation equipment 1.
Specifically, it is in parallel between the high steam input terminal of the vapour compression machine 203 and compression output terminal to be equipped with new steam
Vapour input bypass 404, initial steam input bypass 404 are equipped with bypass flow regulating valve 202, the initial steam input bypass 404
Power flow control valve 201 is equipped between high steam input terminal；Steam flow is installed on first steam conveying pipe 401
Meter 204, bypass flow regulating valve 202 and power flow control valve 201 are according to the feedback flow control steam of steam-flow meter 204
Amount.This structure can realize the flexible control to steam flow, pass through bypass flow regulating valve 202 and power flow control valve 201
Two-stage control is realized to the steam flow of initial steam, by the steam flow of initial steam to limit the first steam conveying pipe 401
Steam flow.
In this way, when the steam flow that steam-flow meter 204 detects is more than setting maximum, bypass flow regulating valve 202
Gradually turn down to adjust the steam flow of the first steam conveying pipe 401, after bypass flow regulating valve 202 is completed to disconnect, steam
Steam flow gauge 204 gradually turns down again still above setting maximum, power flow control valve 201.
The heat exchanger 301 includes setting into vapour chamber 3012, heat exchanging chamber 3011 and steam discharge chamber 3013, the heat exchanging chamber 3011
Put between vapour chamber 3012 and steam discharge chamber 3013, and the heat exchanger into vapour chamber 3012, steam discharge chamber 3013 respectively with setting
Demarcation strip 3015 separates, and is equipped with some heat exchanger tubes 3014 in the heat exchanging chamber 3011, the both ends of the heat exchanger tube 3014 connect respectively
First hot switching path is formed into vapour chamber 3012 and steam discharge chamber 3013 described in logical, second hot switching path, which is arranged on, to be changed
The outside of heat pipe 3014, the upside of heat exchanging chamber 3011 is corresponding to be equipped with steam (vapor) outlet 3017；The steam discharge chamber 3013 is equipped with wine liquid
Outlet (not shown), it is arranged on the downside of steam discharge chamber 3013 and is connected with wine liquid collecting 502, and wine liquid is made in gravity
Wine liquid outlet is flowed under, and wine liquid collecting 502 is discharged to by wine liquid outlet.Second hot switching path is defeated
Enter end and be equipped with atomization box 303, water supplement apparatus is connected with the input terminal of atomization box 303.Atomizer is equipped with the atomization box 303
3031, the second heat exchanger channels are discharged into after water is atomized by the atomizer 3031 again and are exchanged heat with wine vapour, effectively
Improve low-pressure steam formation efficiency.Space of second hot switching path between heat exchanger tube 3014 and heat exchanging chamber 3011, is changed
Helical form deflector 3016, the connection of 3016 outside heat exchanging chamber of helical form deflector, 3011 inner wall, each heat exchange are equipped with hot chamber 3011
Pipe 3014 is each passed through helical form deflector 3016.By setting helical form deflector 3016, water mist is set to pass through helical form water conservancy diversion
The drainage of plate 3016, which is uniformly attached on 3014 outer wall of heat exchanger tube, absorbs thermal energy, makes the first hot switching path and the second hot switching path
Heat exchanger effectiveness higher.
As a preferred solution, the output terminal of second hot switching path passes through low pressure with low-pressure steam input terminal
Steam Recovery pipeline 402 connects, and low-pressure steam recovery channel 402 is equipped with vapour liquid separator 307, vapour liquid separator 307 it is defeated
Enter end to be connected with the output terminal of the second hot switching path, the output terminal of vapour liquid separator 307 is connected with low-pressure steam input terminal, vapour
The drain side of liquid/gas separator 307 is connected with water supplement apparatus.The input terminal of the vapour liquid separator 307 and the second hot switching path
Vacuum blower 306 is equipped between output terminal.In addition, before the output terminal of the vapour liquid separator 307 and low-pressure steam input terminal
Check valve 308 is additionally provided with, the check valve 308 makes the air-flow of low pressure steam line be flowed to the direction of vapour compression machine 203.It is logical
Cross vacuum blower 306 quickly to extract the low-pressure steam in the second heat exchanger channels out, to improve heat exchange efficiency.The water supplement apparatus bag
Water supply tank 302 is included, the drain side is connected with the water supply tank 302 by water return pipeline 603, and the heat of water supply tank 302 and second is handed over
Change path input to connect by moisturizing pipeline 601, the connection of moisturizing pipeline 601 is equipped with heat exchanger 304；The steam discharge chamber
3013 are equipped with steam drain (not shown), and heat exchanger 304 is equipped with the filling pipe input terminal being connected with moisturizing pipeline 601 and benefit
Water pipe output terminal, and the second heat exchange air intake (not shown) and the second heat exchange outlet (not shown), the second heat
Exchange air intake be connected with steam drain, in steam discharge chamber 3013 not liquefied wine vapour through heat exchanger 304 in moisturizing pipeline 601
Wine liquid is generated after water preheating and is discharged from the second heat exchange outlet；Alternatively, the second heat exchange outlet and exterior material
The input terminal connection of pre-heating device, the wine vapour by exterior material pre-heating device and with the material of exterior material pre-heating device into
Row heat exchange, then discharged by the output terminal of exterior material pre-heating device.Preferably, the heat exchanger 304 by filling pipe
The water preheating in road 601 is degree Celsius.It is atomized after the preheating water of heat exchanger 304 into atomization box 303, atomizing effect is more
It is good.
As a preferred solution, the drain side of the vapour liquid separator 307 is provided with steam trap 309 to prevent low pressure
Steam is discharged to water supplement apparatus, and thin drinking vessel 305 is provided with the wine liquid collecting 502 to prevent that uncooled wine vapour from being arranged
To wine liquid collecting 502.
As a preferred solution, the outlet of water supply tank 302 is equipped with high-pressure pump 3021, and the high-pressure pump 3021 exports
It is connected with flowmeter 3023, high-pressure pump 3021 is according to the feedback control rate of water make-up of flowmeter 3023；The water supply tank 302 be equipped with
The inlet channel 602 of external water source connection, is provided with water compensating valve 3022 on inlet channel 602, the external water source passes through moisturizing
Valve 3022 is to 302 automatic water-supply of water supply tank.Preferably, the external water source is soft water source.
Compared with prior art, using the Distallation systm of steam regeneration device 2, steamed using the thermal energy generation low pressure of wine vapour
Vapour, by reducing energy consumption to reduce the distillation cost of white wine, has preferable to reduce the cooling of wine vapour and steam-heated energy consumption
Energy-saving effect.
According to the disclosure and teachings of the above specification, those skilled in the art in the invention can also be to above-mentioned embodiment party
Formula make a change and modification.Therefore, the invention is not limited in embodiment disclosed and described above, to the present invention's
Some modifications and changes should also be as falling into the scope of the claims of the present invention.In addition, although used in this specification
Some specific terms, but these terms are merely for convenience of description, do not limit the present invention in any way.
Claims (10)
- A kind of 1. steam regeneration device using Spirit vapour thermal energy, it is characterised in that：Including vapour compression machine and heat exchanger, The vapour compression machine includes being used for the high steam input terminal, low-pressure steam input terminal and compression output terminal for connecting initial steam, The compression output terminal is connected by the first steam conveying pipe with the steam inlet of distillation equipment；The heat exchanger is equipped with can The first hot switching path and the second hot switching path of heat exchange are carried out, the input terminal of first hot switching path passes through first The wine vapor outlet of wine vapour conveyance conduit and distillation equipment connects, output of the wine vapour through the first hot switching path that distillation equipment produces Enter wine liquid collecting behind end, the input terminal of second hot switching path is used to connect water supplement apparatus, and the second heat exchange is led to The output terminal in road connects the low-pressure steam input terminal；From distillation equipment output wine vapour by during the first hot switching path by the water heating evaporation shape in the second hot switching path Into low-pressure steam, low-pressure steam is passed through distillation equipment after vapour compression machine pressurizes.
- A kind of 2. steam regeneration device using Spirit vapour thermal energy according to claim 1, it is characterised in that：The steaming It is in parallel between the high steam input terminal and compression output terminal of vapour compressor to be equipped with initial steam input bypass, initial steam input bypass Bypass flow regulating valve is equipped with, power flow-rate adjustment is equipped between the initial steam input bypass and high steam input terminal Valve；Steam-flow meter is installed, bypass flow regulating valve and power flow control valve are according to steam on the first steam conveying pipe The feedback flow control of flowmeter corresponds to the quantity of steam of pipeline.
- A kind of 3. steam regeneration device using Spirit vapour thermal energy according to claim 1, it is characterised in that：The heat Exchanger is included into vapour chamber, heat exchanging chamber and steam discharge chamber, and the heat exchanging chamber is arranged on between vapour chamber and steam discharge chamber, the heat exchanging chamber Interior to be equipped with some heat exchanger tubes, the both ends of the heat exchanger tube are respectively communicated with described forms first heat exchange into vapour chamber and steam discharge chamber Passage, second hot switching path are arranged on the outside of heat exchanger tube；The steam discharge chamber has wine liquid outlet, wine liquid outlet It is connected with wine liquid collecting.
- A kind of 4. steam regeneration device using Spirit vapour thermal energy according to claim 3, it is characterised in that：Described Two hot switching path input terminals are equipped with atomization box, the input terminal connection of water supplement apparatus and atomization box.
- 5. a kind of steam regeneration device using Spirit vapour thermal energy according to any one of claims 1 to 4, its feature exist In：The output terminal of second hot switching path is connected with low-pressure steam input terminal by low-pressure steam recovery channel, and low pressure is steamed Vapour recovery channel is equipped with vapour liquid separator, and the input terminal of vapour liquid separator is connected with the output terminal of the second hot switching path, vapour The output terminal of liquid/gas separator is connected with low-pressure steam input terminal, and the drain side of vapour liquid separator is connected with water supplement apparatus.
- A kind of 6. steam regeneration device using Spirit vapour thermal energy according to claim 5, it is characterised in that：The vapour Vacuum blower is equipped between the output terminal of the input terminal of liquid/gas separator and the second hot switching path.
- A kind of 7. steam regeneration device using Spirit vapour thermal energy according to claim 3 or 4, it is characterised in that：Institute Stating water supplement apparatus includes water supply tank, and water supply tank is connected with the second hot switching path input terminal by water pipe, and water pipe connects Connect and be equipped with second heat exchanger；The steam discharge chamber is equipped with steam drain, and second heat exchanger is equipped with what is be connected with water pipe Filling pipe input terminal and filling pipe output terminal, and the second heat exchange air intake and the second heat exchange outlet, the second heat exchange Air intake is connected with steam drain, and not liquefied wine vapour preheats the water in filling pipe through second heat exchanger in steam discharge chamber；The output terminal of second hot switching path is connected with low-pressure steam input terminal by low-pressure steam recovery channel, and low pressure is steamed Vapour recovery channel is equipped with vapour liquid separator, and the input terminal of vapour liquid separator is connected with the output terminal of the second hot switching path, vapour The output terminal of liquid/gas separator is connected with low-pressure steam input terminal, and the drain side of vapour liquid separator is connected with water supplement apparatus.
- A kind of 8. steam regeneration device using Spirit vapour thermal energy according to claim 3 or 4, it is characterised in that：Institute Space of second hot switching path between heat exchanger tube and heat exchanging chamber is stated, is equipped with helical form deflector in heat exchanging chamber, helical form is led The connection of heat exchange cavity wall, each heat exchanger tube are each passed through helical form deflector on the outside of flowing plate.
- A kind of 9. steam regeneration device using Spirit vapour thermal energy according to claim 5, it is characterised in that：The vapour The drain side of liquid/gas separator is provided with steam trap, and thin drinking vessel is provided with the wine liquid collecting.
- A kind of 10. steam regeneration device using Spirit vapour thermal energy according to claim 7, it is characterised in that：It is described Water supply tank outlet is equipped with high-pressure pump, and the high pressure pump outlet is connected with flowmeter, and high-pressure pump is mended according to the feedback control of flowmeter Water；The water supply tank is equipped with the inlet channel being connected with external water source, and water compensating valve is provided with inlet channel.
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| CN201810026786.2A CN107937228A (en) | 2018-01-11 | 2018-01-11 | A kind of steam regeneration device using Spirit vapour thermal energy |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113388484A (en) * | 2021-08-05 | 2021-09-14 | 佛山市丰川节能科技有限公司 | White spirit distillation system and distillation method |
| CN114214161A (en) * | 2021-12-08 | 2022-03-22 | 广东省九江酒厂有限公司 | Energy-saving distillation device and distillation method for white spirit |
| CN114607998A (en) * | 2022-04-14 | 2022-06-10 | 泸州老窖股份有限公司 | Bran steaming waste gas heat energy recovery processing method and bran steaming machine system used for same |
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| CN114214161A (en) * | 2021-12-08 | 2022-03-22 | 广东省九江酒厂有限公司 | Energy-saving distillation device and distillation method for white spirit |
| CN114607998A (en) * | 2022-04-14 | 2022-06-10 | 泸州老窖股份有限公司 | Bran steaming waste gas heat energy recovery processing method and bran steaming machine system used for same |
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