CN206459377U - A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house - Google Patents
A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house Download PDFInfo
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- CN206459377U CN206459377U CN201621378456.2U CN201621378456U CN206459377U CN 206459377 U CN206459377 U CN 206459377U CN 201621378456 U CN201621378456 U CN 201621378456U CN 206459377 U CN206459377 U CN 206459377U
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Abstract
The utility model provides a kind of high-efficiency condensation system dehumidified for tobacco flue-curing house, and the high-efficiency condensation system includes the dehydrating unit, the cold water tank with dehydrating unit formation water circulation, the refrigerating plant cooled down with the water in the heat exchange tank and heat exchanging tank of cold water tank formation water circulation for being used to dehumidify to the damp-heat air in tobacco flue-curing house；Cold water tank is provided with the first delivery port being connected with dehydrating unit and the first water inlet and exchange heat tank connected second delivery port and the second water inlet；The the first heat conduction chamber and the second heat conduction chamber being arranged in the first thermal conductive cavity room and the 3rd heat conduction chamber for buffering water temperature change are additionally provided with cold water tank.By above-mentioned setting, the utility model greatly reduces the working strength of refrigerating plant, so as to reduce energy consumption, and ensure that the effect on moisture extraction of dehydrating unit and the cooling effect of heat exchange tank.
Description
Technical field
The utility model is related to tobacco flue-curing house field, more particularly, to a kind of high-efficiency condensation system dehumidified for tobacco flue-curing house
System.
Background technology
Tobacco flue-curing house is indispensable basic equipment in cured tobacco production.Tobacco flue-curing house is just shown after interior baking modulation
The distinctive color of flue-cured tobacco, type, as the quality raw materials for meeting cigarette industry needs, its general principle be tobacco leaf it is heated after,
Moisture discharge in tobacco leaf, is discharged outside tobacco flue-curing house after moisture vaporization, so that tobacco leaf scalding, drying.But tobacco flue-curing house is wet
Heat and fragrance have been taken away when hot gas is discharged, the circulation of the energy is have impact on, the waste of energy is caused.In order to solve
This problem, people set dehydrating unit in tobacco flue-curing house, and dehydrating unit to the steam in hot and humid gas condense reaching
To the effect of dehumidifying, while fragrance is remained in tobacco flue-curing house.But the refrigerator in dehydrating unit is needed during flue-cured tobacco
Run always, and in order to which steam can be condensed in a short time, it is necessary to maintain relatively low cryogenic temperature, so cause dehumidifying
The energy consumption of device is higher.
Utility model content
The utility model is that the defect for overcoming above-mentioned prior art is used for the high-efficiency condensation system that tobacco flue-curing house dehumidifies there is provided a kind of
System, the high-efficiency condensation system effectively can dehumidify to the hot and humid gas in tobacco flue-curing house, while energy when can reduce dehumidifying
Consumption.
In order to solve the above technical problems, the technical solution adopted in the utility model is：
A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house, including for being dehumidified to the damp-heat air in tobacco flue-curing house
Dehydrating unit, with the dehydrating unit formation water circulation cold water tank, with the cold water tank formation water circulation heat exchange tank, with
And the refrigerating plant that the water in heat exchanging tank is cooled down；The cold water tank be provided with the first delivery port for being connected with dehydrating unit and
First water inlet and exchange heat tank connected second delivery port and the second water inlet；
The first heat conduction chamber for buffering water temperature change is additionally provided with the cold water tank and the first thermal conductive cavity is arranged on
Indoor the second heat conduction chamber and the 3rd heat conduction chamber, the second heat conduction chamber is connected with first water inlet；Described
Three heat conduction chambers are connected with second water inlet；The first gap that the first heat conduction chamber overflows provided with supplying water, it is described
Second heat conduction chamber and the 3rd heat conduction chamber are respectively equipped with the second gap and the 3rd gap for supplying water and overflowing, and described first overflows
The level height at the mouth of a river is higher than the liquid level of the cold water tank；The level height of second gap and the 3rd gap is high
In the level height of first gap.
On the one hand, cold water tank carries out water circulation with the dehydrating unit, directly provides low-temperature receiver, the opposing party for dehydrating unit
Face, cold water tank is carried out in water circulation with the heat exchange tank, and the water of cold water tank can further be cooled down at heat exchange tank, cooling
Rear water is neutralized with the water after dehumidifying heat absorption in cold water tank so that the water in cold water tank is able to maintain that in certain temperature range,
Make the effect on moisture extraction of dehydrating unit stable.Due to the water after refrigerating plant dehumidifying heat absorption directly not higher to temperature carry out it is cold
But, but the water in the cold water tank relatively low to script temperature is cooled down, so substantially reduce the working strength of refrigerating plant, from
And reduce energy consumption.
In addition, by setting the first heat conduction chamber, the second heat conduction chamber, the 3rd heat conduction chamber so that dehumidifying is heated
Recirculation water afterwards flows separately through the second heat conduction chamber and the 3rd heat conduction chamber with the water after being cooled down through the heat exchange tank, and in this phase
Between with outside the chamber（That is in the first thermal conductive cavity room）Water carry out heat exchange, mixed again in the first thermal conductive cavity room afterwards
Close, preferably carry out heat exchange, the water after heat exchange flows into cold water tank at first gap again, so can
Influence of the water temperature change to cold water tank is reduced so that the water temperature of cold water tank is stablized relatively, so as to ensure the dehumidifying effect of dehydrating unit
Fruit and the cooling effect of heat exchange tank.
Further, first water inlet is connected with the bottom of the second heat conduction chamber, the second gap position
In the top of the second heat conduction chamber；Second water inlet is connected with the bottom of the 3rd heat conduction chamber, and the described 3rd
Gap is located at the top of the 3rd heat conduction chamber.
Further, the dehydrating unit is provided with for the first passage of cold water flow and for the damp and hot airflow of tobacco flue-curing house
Second channel；The mutual heat exchange of air-flow of cold water and second channel in the first passage；
The first passage is provided with the first input port and the first delivery outlet, first input port and the first delivery outlet difference
It is connected with first delivery port and the first water inlet, so that the cold water tank and dehydrating unit formation water circulation system.It is described
Second channel is connected with tobacco flue-curing house.
In order to which water circulation is better achieved, to reach more preferable heat transfer effect, further, first input port with
The junction of first delivery port is provided with the second pump.
Further, the heat exchange tank is provided with the second input port and the second delivery outlet, second input port and second defeated
Outlet is connected with second delivery port and the second water inlet respectively, so that the cold water tank and heat exchange tank formation water circulation system
System.In order to which water circulation is better achieved, to reach more preferable heat transfer effect, further, second delivery port and second
The junction of input port is provided with the first pump.
Further, the refrigerating plant include head and the tail be sequentially connected and form the evaporator of heat exchange circulation, capillary,
Condenser, compressor；The evaporator, capillary, condenser, compressor constitute closed cycle system by placed in series；Institute
Evaporator is stated to be arranged in the heat exchange tank.The refrigerating plant uses the principle similar to air conditioner refrigerating, and refrigerant is in evaporation
Evaporation endothermic in device, is cooled down with the water in heat exchanging tank.
In order to improve the utilization rate of energy, further, the condenser is arranged in tobacco flue-curing house, with to tobacco flue-curing house
It is internally heated.
Compared with prior art, the beneficial effects of the utility model are：
The high-efficiency condensation system described in the utility model dehumidified for tobacco flue-curing house, by setting respectively with dehydrating unit and changing
The cold water tank of hot tank formation water circulation so that refrigerating plant carries out cold without the water after dehumidifying heat absorption directly higher to temperature
But, but the water in the cold water tank relatively low to script temperature is cooled down, so substantially reduce the working strength of refrigerating plant, from
And reduce energy consumption.And first delivery port and the second delivery port are arranged on to the bottom of cold water tank, described first is intake
Mouth and the second water inlet are arranged on the top of cold water tank so that the water temperature of cold water pot bottom is stablized relatively, so as to ensure dehumidifying dress
The effect on moisture extraction and the cooling effect of heat exchange tank put.
Brief description of the drawings
Fig. 1 is to be used for the structural representation for the high-efficiency condensation system that tobacco flue-curing house dehumidifies described in embodiment 1.
Fig. 2 is the local structural representation of cold water tank described in embodiment 1.
Fig. 3 is to be used for the structural representation for the high-efficiency condensation system that tobacco flue-curing house dehumidifies described in embodiment 2.
Embodiment
The utility model is further described with reference to embodiment.
The same or analogous part of same or analogous label correspondence in the accompanying drawing of the utility model embodiment；In this practicality
In new description, it is to be understood that if thering is term " on ", " under ", "left", "right", " top ", " bottom ", " interior ", " outer " etc. to refer to
The orientation or position relationship shown be based on orientation shown in the drawings or position relationship, be for only for ease of description the utility model and
Simplify description, rather than indicate or imply that the device or element of meaning there must be specific orientation, with specific azimuth configuration
And operation, therefore described in accompanying drawing position relationship term being given for example only property explanation, it is impossible to be interpreted as the limitation to this patent.
If in addition, there is the term such as " first ", " second " to be only used for describing purpose, be mainly used for distinguishing different devices,
Element or part（Specific species is identical with construction possibility may also be different）, it is not intended to show or implies indicated dress
Put, the relative importance and quantity of element or part, and it is not intended that indicating or implying relative importance.
Embodiment 1
It is as shown in Figure 1 and 2 a kind of embodiment of the high-efficiency condensation system dehumidified for tobacco flue-curing house of the utility model, it is described
High-efficiency condensation system includes the dehydrating unit 100 and dehydrating unit for being used to dehumidify to the damp-heat air in tobacco flue-curing house 700
100 form the cold water tank 300 of water circulation, are formed with cold water tank 300 in the heat exchange tank 200 and heat exchanging tank 200 of water circulation
The refrigerating plant 400 that water is cooled down.
Specifically, cold water tank 300 is provided with the first delivery port 301 and the first water inlet being connected with dehydrating unit 100
302nd, the second delivery port 303 and the second water inlet 304 being connected with heat exchange tank 200, the first delivery port 301 and the second delivery port
303 are arranged on the bottom of cold water tank, and the first water inlet 302 and the second water inlet 304 are arranged on the top of cold water tank 300, first
The water inlet 304 of water inlet 302 and second is located at the homonymy of cold water tank 300.
The first heat conduction chamber 305 for buffering water temperature change is additionally provided with cold water tank 300 and the first heat conduction is arranged on
The second heat conduction chamber 306 and the 3rd heat conduction chamber 307 in chamber, the bottom of the second heat conduction chamber 306 and the first water inlet 302
Connection, the bottom of the 3rd heat conduction chamber 307 is connected with the second water inlet 304, and the top of the first heat conduction chamber is overflowed provided with supplying water
The first gap 308, the top of the second heat conduction chamber and the top of the 3rd heat conduction chamber are respectively equipped with second for supplying water and overflowing
The gap 310 of gap 309 and the 3rd.The level height of first gap is higher than the liquid level of cold water tank 300, the second spilling water
The level height of mouth and the 3rd gap is higher than the level height of the first gap.
Dehydrating unit 100 is provided with second for the first passage 101 of cold water flow and for the damp and hot airflow of tobacco flue-curing house
The mutual heat exchange of air-flow of cold water and second channel 102 in passage 102, first passage 101.
First passage 101 is provided with the first input port 103 and the first delivery outlet 104, the first input port 103 and the first delivery outlet
104 are connected with the first delivery port 301 and the first water inlet 302 respectively, so that cold water tank 300 and dehydrating unit formation water circulation system
System.First input port 103 and the junction of the first delivery port are provided with the second pump 600.
Heat exchange tank 200 is provided with the second input port 201 and the second delivery outlet 202, the second input port 201 and the second delivery outlet
202 are connected with the second delivery port 303 and the second water inlet 304 respectively, so that cold water tank and the formation water circulation of heat exchange tank 200 system
System.The junction of second delivery port 303 and the second input port 201 is provided with the first pump 500.
First delivery port 301 and the second delivery port 303 are arranged on to the bottom of cold water tank 300 simultaneously, by the first water inlet
302 and second water inlet 304 be arranged on the top of cold water tank, the water temperature of such bottom of cold water tank 300 is stablized relatively, so as to ensure
The effect on moisture extraction of dehydrating unit 100 and the cooling effect of heat exchange tank 200.
Refrigerating plant, which can be used, can realize the prior art of refrigerating function.
On the one hand, cold water tank carries out water circulation with dehydrating unit, directly provides low-temperature receiver for dehydrating unit, on the other hand, cold
Water pot carries out water circulation with heat exchange tank, and the water of cold water tank can further be cooled down at heat exchange tank, and the water after cooling is with removing
Water after wet heat absorption is being neutralized so that the water in cold water tank is able to maintain that in certain temperature range.Because refrigerating plant is not straight
The water after higher to temperature dehumidifying heat absorption is connect to cool down, but the water progress in the cold water tank relatively low to script temperature is cold
But, the working strength of refrigerating plant is so substantially reduced, so as to reduce energy consumption.
Embodiment 2
A kind of another embodiment of the high-efficiency condensation system dehumidified for tobacco flue-curing house of the utility model is illustrated in figure 3,
In the present embodiment, refrigerating plant 400 includes evaporator 401, the capillary that head and the tail were sequentially connected and formed heat exchange circulation
402nd, condenser 404, compressor 403, evaporator 401 are arranged in heat exchange tank, and condenser 404 is arranged in tobacco flue-curing house.The system
Device for cooling uses the principle similar to air conditioner refrigerating, and refrigerant evaporation endothermic in evaporator is entered with the water in heat exchanging tank 200
Row cooling, refrigerant condenses heat release within the condenser, to be internally heated to tobacco flue-curing house, can so effectively improve energy
Utilization rate.
Obviously, above-described embodiment of the present utility model is only intended to clearly illustrate the utility model example, and
It is not the restriction to embodiment of the present utility model.For those of ordinary skill in the field, in described above
On the basis of can also make other changes in different forms.There is no need and unable to give all embodiments
It is exhaustive.All any modifications, equivalent substitutions and improvements made within spirit of the present utility model and principle etc., should be included in
Within the utility model scope of the claims.
Claims (7)
1. a kind of high-efficiency condensation system dehumidified for tobacco flue-curing house, it is characterised in that including for the damp and hot sky in tobacco flue-curing house
The dehydrating unit that gas is dehumidified（100）And the cold water tank of dehydrating unit formation water circulation（300）And the cold water tank
（300）Form the heat exchange tank of water circulation（200）And heat exchanging tank（200）The refrigerating plant that interior water is cooled down（400）；
The cold water tank（300）Provided with the first delivery port being connected with dehydrating unit（301）With the first water inlet（302）With heat exchange tank
（200）Second delivery port of connection（303）With the second water inlet（304）；
The cold water tank（300）Inside it is additionally provided with the first heat conduction chamber for buffering water temperature change（305）And it is arranged on first
Heat conduction chamber（305）The second interior heat conduction chamber（306）With the 3rd heat conduction chamber（307）, the second heat conduction chamber with it is described
First water inlet is connected；The 3rd heat conduction chamber is connected with second water inlet；The first heat conduction chamber（305）It is provided with
Supply water the first gap overflowed（308）, the second heat conduction chamber and the 3rd heat conduction chamber are respectively equipped with for supplying water and overflowing
Two gaps（309）With the 3rd gap（310）, the level height of first gap is higher than the cold water tank（300）'s
Liquid level；The level height of second gap and the 3rd gap is higher than the level height of first gap.
2. high-efficiency condensation system according to claim 1, it is characterised in that the dehydrating unit（100）Provided with cooling water
The first passage of flowing（101）With the second channel for the damp and hot airflow of tobacco flue-curing house（102）；The first passage（101）
In cold water and second channel（102）The mutual heat exchange of air-flow；
The first passage（101）Provided with the first input port（103）With the first delivery outlet（104）, first input port（103）
With the first delivery outlet（104）Respectively with first delivery port（301）With the first water inlet（302）Connection, so that the cold water
Tank（300）With dehydrating unit（100）Form water circulation system.
3. high-efficiency condensation system according to claim 2, it is characterised in that first input port（103）Go out with first
The mouth of a river（301）Junction be provided with the second pump（600）.
4. high-efficiency condensation system according to claim 1, it is characterised in that the heat exchange tank（200）Provided with the second input
Mouthful（201）With the second delivery outlet（202）, second input port（201）With the second delivery outlet（202）Go out respectively with described second
The mouth of a river（301）With the second water inlet（304）Connection, so that the cold water tank（300）With heat exchange tank（200）Form water circulation system
System.
5. high-efficiency condensation system according to claim 4, it is characterised in that second delivery port（303）It is defeated with second
Entrance（201）Junction be provided with the first pump（500）.
6. high-efficiency condensation system according to claim 1, it is characterised in that the refrigerating plant（400）Including head and the tail according to
The secondary evaporator for connecting and forming heat exchange circulation（401）, capillary（402）, condenser（404）, compressor（403）；It is described
Evaporator（401）, capillary（402）, condenser（404）, compressor（403）Closed cycle system is constituted by placed in series；
The evaporator（401）It is arranged on the heat exchange tank（200）It is interior.
7. high-efficiency condensation system according to claim 6, it is characterised in that the condenser（404）It is arranged on tobacco flue-curing house
It is interior, to be internally heated to tobacco flue-curing house.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378456.2U CN206459377U (en) | 2016-12-15 | 2016-12-15 | A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378456.2U CN206459377U (en) | 2016-12-15 | 2016-12-15 | A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206459377U true CN206459377U (en) | 2017-09-01 |
Family
ID=59697752
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621378456.2U Expired - Fee Related CN206459377U (en) | 2016-12-15 | 2016-12-15 | A kind of high-efficiency condensation system dehumidified for tobacco flue-curing house |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206459377U (en) |
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2016
- 2016-12-15 CN CN201621378456.2U patent/CN206459377U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170901 Termination date: 20191215 |
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| CF01 | Termination of patent right due to non-payment of annual fee |