CN206443181U - A kind of condenser system dehumidified for tobacco flue-curing house - Google Patents
A kind of condenser system dehumidified for tobacco flue-curing house Download PDFInfo
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- CN206443181U CN206443181U CN201621378458.1U CN201621378458U CN206443181U CN 206443181 U CN206443181 U CN 206443181U CN 201621378458 U CN201621378458 U CN 201621378458U CN 206443181 U CN206443181 U CN 206443181U
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- tank
- water
- cold water
- heat exchange
- dehydrating unit
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Abstract
The utility model provides a kind of condenser system dehumidified for tobacco flue-curing house, and the condenser 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 chamber for buffering water temperature change is additionally provided with cold water tank, chamber is connected with first water inlet and the second water inlet respectively；The gap that chamber overflows provided with supplying water, the level height of gap is higher than the liquid level of cold water tank.By above-mentioned setting, the utility model greatly reduces the working strength of refrigerating plant, so as to reduce energy consumption so that the water temperature of cold water tank is stablized relatively, so as to ensure 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 condenser system dehumidified for tobacco flue-curing house.
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 condenser system that tobacco flue-curing house dehumidifies there is provided a kind of,
The condenser system effectively can dehumidify to the hot and humid gas in tobacco flue-curing house, while energy consumption when can reduce dehumidifying.
In order to solve the above technical problems, the technical solution adopted in the utility model is：
A kind of condenser system dehumidified for tobacco flue-curing house, including for removing for being dehumidified to the damp-heat air in tobacco flue-curing house
Wet device, the cold water tank with dehydrating unit formation water circulation, with the cold water tank form the heat exchange tank of water circulation and right
The refrigerating plant that water in heat exchange tank is cooled down；The cold water tank is provided with the first delivery port and first being connected with dehydrating unit
Water inlet and exchange heat tank connected second delivery port and the second water inlet；It is additionally provided with the cold water tank for buffering water temperature change
The chamber of change, the chamber is connected with first water inlet and the second water inlet respectively；The chamber is provided with the spilling that supplies water
Gap, the level height of the gap is higher than the liquid level of the cold water tank.
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
Water afterwards is being neutralized with the water after dehumidifying heat absorption so that the water in cold water tank is able to maintain that in certain temperature range, makes dehumidifying
The effect on moisture extraction of device is stable.Because the water after refrigerating plant dehumidifying heat absorption directly not higher to temperature is cooled down, but
Water in the cold water tank relatively low to script temperature is cooled down, and so substantially reduces the working strength of refrigerating plant, so as to reduce
Energy consumption.
In addition, by setting the chamber so that the recirculation water after dehumidifying is heated and the water after heat exchange tank cooling
It can be mixed in advance in chamber, preferably carry out heat exchange, the water after heat exchange is again at the gap
Cold water tank is flowed into, influence of the water temperature change to cold water tank can be so reduced so that the water temperature of cold water tank is stablized relatively, so as to protect
Demonstrate,prove the effect on moisture extraction of dehydrating unit and the cooling effect of heat exchange tank.
Further, first water inlet and the second water inlet are connected with the bottom of the chamber, the gap position
In the top of the chamber.
Further, the outer surface of the chamber is provided with thermal insulation layer, to reduce the change of chamber interior water temperature to exterior thereto
The influence of water temperature.
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：
It is described in the utility model for tobacco flue-curing house dehumidify condenser system, by set respectively with dehydrating unit and heat exchange tank
Form the cold water tank of water circulation so that refrigerating plant is cooled down without the water after dehumidifying heat absorption directly higher to temperature, and
It is that water in the cold water tank relatively low to script temperature is cooled down, the working strength of refrigerating plant is so substantially reduced, so as to drop
Low energy consumption.And by setting the chamber so that the recirculation water after dehumidifying is heated and the water energy after heat exchange tank cooling
It is enough to be mixed in advance in chamber, heat exchange is preferably carried out, the water after heat exchange flows at the gap again
Enter cold water tank, can so reduce influence of the water temperature change to cold water tank so that the water temperature of cold water tank is stablized relatively, so as to ensure
The effect on moisture extraction of dehydrating unit and the cooling effect of heat exchange tank.
Brief description of the drawings
Fig. 1 is to be used for the structural representation for the condenser 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 condenser system that tobacco flue-curing house dehumidifies described in embodiment 2.
Fig. 4 is the local structural representation of cold water tank 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 condenser system dehumidified for tobacco flue-curing house of the utility model, the condensation
System includes the dehydrating unit 100 and the formation water of dehydrating unit 100 for being used to dehumidify to the damp-heat air in tobacco flue-curing house 700
The cold water tank 300 of circulation, with cold water tank 300 formation water circulation heat exchange tank 200 and heat exchanging tank 200 in water carry out it is cold
But refrigerating plant 400.
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 chamber 305 for buffering water temperature change is additionally provided with cold water tank 300, the bottom of chamber 305 is entered with first respectively
The mouth of a river and the connection of the second water inlet, gap 306 of the top provided with the spilling that supplies water of chamber 305, the level height of gap 306
Higher than the liquid level of cold water tank.
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
As Fig. 3 ~ 4 are shown, the utility model is a kind of to be used for another embodiment for the condenser system that tobacco flue-curing house dehumidifies,
In the present embodiment, the outer surface of the chamber 305 in cold water tank 300 is provided with thermal insulation layer 307, to reduce the change pair of chamber interior water temperature
The influence of exterior thereto water temperature.
Refrigerating plant 400 includes being sequentially connected and being formed the evaporator 401 of heat exchange circulation, capillary 402, condensation from beginning to end
Device 404, compressor 403, evaporator 401 are arranged in heat exchange tank, and condenser 404 is arranged in tobacco flue-curing house.The refrigerating plant is adopted
With the principle similar to air conditioner refrigerating, refrigerant evaporation endothermic in evaporator is cooled down with the water in heat exchanging tank 200,
Refrigerant condenses heat release within the condenser, to be internally heated to tobacco flue-curing house, can so effectively improve the utilization of energy
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 (8)
1. a kind of condenser system dehumidified for tobacco flue-curing house, it is characterised in that including for entering to the damp-heat air in tobacco flue-curing house
The dehydrating unit of row dehumidifying（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）；It is described cold
Water pot（300）Provided with the first delivery port being connected with dehydrating unit（301）With the first water inlet（302）With heat exchange tank（200）Even
The second delivery port connect（303）With the second water inlet（304）；The cold water tank（300）Inside it is additionally provided with for buffering water temperature change
Chamber（305）, the chamber（305）Respectively with first water inlet（301）With the second water inlet（304）Connection；It is described
Chamber（305）The gap overflowed provided with supplying water（306）, the level height of the gap is higher than the cold water tank（300）'s
Liquid level.
2. condenser system according to claim 1, it is characterised in that the chamber（305）Outer surface be provided with thermal insulation layer
（307）.
3. condenser system according to claim 1, it is characterised in that the dehydrating unit（100）Provided with supplying cold water flow
First passage（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.
4. condenser system according to claim 3, it is characterised in that first input port（103）With the first delivery port
（301）Junction be provided with the second pump（600）.
5. condenser system according to claim 1, it is characterised in that the heat exchange tank（200）Provided with the second input port
（201）With the second delivery outlet（202）, second input port（201）With the second delivery outlet（202）Respectively with second water outlet
Mouthful（301）With the second water inlet（304）Connection, so that the cold water tank（300）With heat exchange tank（200）Form water circulation system.
6. condenser system according to claim 5, it is characterised in that second delivery port（303）With the second input port
（201）Junction be provided with the first pump（500）.
7. condenser system according to claim 1, it is characterised in that the refrigerating plant（400）Connect successively including head and the tail
Connect and formed the evaporator of heat exchange circulation（401）, capillary（402）, condenser（404）, compressor（403）；The evaporation
Device（401）, capillary（402）, condenser（404）, compressor（403）Closed cycle system is constituted by placed in series；It is described
Evaporator（401）It is arranged on the heat exchange tank（200）It is interior.
8. condenser system according to claim 7, it is characterised in that the condenser（404）It is arranged in tobacco flue-curing house, with
Tobacco flue-curing house is internally heated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378458.1U CN206443181U (en) | 2016-12-15 | 2016-12-15 | A kind of condenser system dehumidified for tobacco flue-curing house |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378458.1U CN206443181U (en) | 2016-12-15 | 2016-12-15 | A kind of condenser system dehumidified for tobacco flue-curing house |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206443181U true CN206443181U (en) | 2017-08-29 |
Family
ID=59672816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621378458.1U Expired - Fee Related CN206443181U (en) | 2016-12-15 | 2016-12-15 | A kind of condenser system dehumidified for tobacco flue-curing house |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206443181U (en) |
-
2016
- 2016-12-15 CN CN201621378458.1U patent/CN206443181U/en not_active Expired - Fee Related
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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: 20170829 Termination date: 20191215 |