CN206443182U - A kind of tobacco flue-curing house - Google Patents
A kind of tobacco flue-curing house Download PDFInfo
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- CN206443182U CN206443182U CN201621378465.1U CN201621378465U CN206443182U CN 206443182 U CN206443182 U CN 206443182U CN 201621378465 U CN201621378465 U CN 201621378465U CN 206443182 U CN206443182 U CN 206443182U
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Abstract
The utility model is related to the technical field of flue-cured tobacco, more particularly, to a kind of tobacco flue-curing house.A kind of tobacco flue-curing house, wherein, the refrigeration system being connected including the dehumidification system being dehumidified tobacco roasting, with dehumidification system, in addition to heating system, heat-exchange system, described heat-exchange system is located to be connected between refrigeration system and heating system and respectively with refrigeration system, heating system；Also include the blower system in tobacco roasting, and improving the temperature elevation system of temperature tobacco roasting, described heat-exchange system includes the second capillary, the second evaporator, the second compressor and condenser, and second capillary, the second evaporator, condenser and the second compressor constitute closed cycle system by placed in series.The utility model heat-exchange system is provided with some assisted capillaries and induction installation, so sets and according to circumstances can carry out heat exchange, and the speed that adjustment is exchanged in real time, improve the efficiency and validity of heat exchange.
Description
Technical field
The utility model is related to the technical field of flue-cured tobacco, more particularly, to a kind of 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.
Heat and fragrance have been taken away when but the hot and humid gas of tobacco flue-curing house are discharged, the circulation of the energy has been have impact on, makes
Into the waste of energy.Now many tobacco flue-curing houses all be directed to solve this respect the problem of, but can Efficient Cycle utilize
The method and equipment of hot and humid gas energy are seldom, and cost of equipment is high and application method is generally more complicated, and practicality is low.
Utility model content
The utility model is to overcome at least one defect described in above-mentioned prior art there is provided a kind of tobacco flue-curing house, and heat energy is sharp
High with rate, a water outlet is without going out fragrance；And fast and effectively the hot and humid gas tobacco roasting can be dehumidified, it can follow
Ring utilizes the heat energy of hot and humid gas, and heat-exchange system is controllable, improves the efficiency of heat exchange；And heat-exchange system is provided with some
Assisted capillary and induction installation, so setting according to circumstances can carry out heat exchange, and the speed that adjustment is exchanged in real time,
Improve the efficiency and validity of heat exchange.
In order to solve the above technical problems, the technical solution adopted in the utility model is：A kind of tobacco flue-curing house, wherein, including it is right
The dehumidification system dehumidified between tobacco roasting, the refrigeration system being connected with dehumidification system, in addition to heating system, heat exchange series
System, described heat-exchange system is located to be connected between refrigeration system and heating system and respectively with refrigeration system, heating system；
Also include the blower system in tobacco roasting, and improving the temperature elevation system of temperature tobacco roasting；
Described heat-exchange system includes the second capillary, the second evaporator, the second compressor and condenser, described the
Two capillaries, the second evaporator, condenser and the second compressor constitute closed cycle system by placed in series；
Some assisted capillaries of second capillary paralleling, it is auxiliary that the parallel branch of the assisted capillary is provided with control
The control device of capillary working condition is helped, the heat-exchange system also includes being used to sense refrigeration system and heating system temperature
Induction installation, the induction installation and control device.
Specifically, described dehumidification system includes the 3rd heat exchanger, the dehumidifying dress for air-flow heat exchange and air inlet
Put and the second blower fan for the air-flow after dehumidifying to be inputted between tobacco roasting；3rd heat exchanger is provided with for damp and hot
The second channel that the first passage of airflow and dry and cold air-flow or xeothermic air-flow pass through, the dehydrating unit, which is provided with, to be used for wet
The third channel for the cold water flow that thermal current is dehumidified and the fourth lane for damp and hot airflow, the first passage with
Fourth lane is connected, the air-flow of the first passage and the mutual heat exchange of the air-flow of second channel；3rd heat exchanger is provided with use
The second entrance flowed into the damp and hot air-flow of baking room；Described dehydrating unit connection refrigeration system.
In the utility model, pass through the 3rd heat exchanger, dehydrating unit and the use for air-flow heat exchange and air inlet
The setting of blower fan between the air-flow input tobacco roasting after by dehumidifying so that dehumidification system utilizes heat transfer, by hot and humid gas
Heat recycled in the 3rd heat exchanger, and hot and humid gas are dehumidified using dehydrating unit, will be dehumidified using blower fan
System processing after gas be re-circulated between tobacco roasting, realize the circulation of energy and gas, it is to avoid energy dissipation with
And fragrance overflows.It is easy to use and cost is low and the dehumidification system between tobacco roasting of the present utility model is simple in construction.
Further, described refrigeration system includes the cold water tank with dehydrating unit formation water circulation, the cold water
Tank is provided with the first delivery port and the first water inlet being connected with dehydrating unit；First water inlet and the first delivery port are arranged on
The top of cold water tank；
The third channel 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
First input port and the junction of the first delivery port are provided with the 3rd pump；Described cold water tank connection heat-exchange system.
In the utility model, on the one hand, cold water tank carries out water circulation with the dehydrating unit, is directly provided for dehydrating unit
Low-temperature receiver, on the other hand, cold water tank are carried out in water circulation with first heat exchange tank, and the water of cold water tank can be at the first heat exchange tank
Further cooled down, the water after cooling is being neutralized with the water after dehumidifying heat absorption so that the water in cold water tank is able to maintain that one
Fixed temperature range.
Further, the cold water tank is provided with the display device for being used for showing cold water tank water level, and the dehumidification system leads to
Cross demountable structure and be installed on tobacco flue-curing house.
In the utility model, the cold water tank is provided with the display device for being used for showing cold water tank water level, the dehumidifying system
System is installed on tobacco flue-curing house by demountable structure, and it is for the ease of observing the water level of cold water tank, so as to cold water tank energy so to set
It is enough that the low-temperature receiver of dehydrating unit is preferably provided, and be easy to the maintenance of dehumidification system and install and use.
Further, described heat-exchange system includes the second capillary, the second evaporator, the second compressor and condensation
Device, second capillary, the second evaporator, condenser and the second compressor constitute closed cycle system by placed in series；
The heat-exchange system is also including for accommodating the second heat exchange tank of condenser and for accommodating the second evaporator
First heat exchange tank；First heat exchange tank is provided with the second input port and the second delivery outlet, second input port and the second delivery outlet point
It is not connected with the second delivery port of cold water pot bottom and the second water inlet of cold water tank sidepiece, so that the cold water tank is changed with first
Hot tank formation water circulation system；The junction of second delivery port and the second input port is provided with the second pump.
The heat-exchange system that the utility model is provided is sequentially connected the second capillary, the second evaporator, condensation by pipeline
Device and compressor form in the closed circulatory system, first heat exchange tank and the second heat exchange tank and are contained with water, the condenser
In the water for being immersed in the second heat exchange tank, second evaporator is immersed in the water of the first heat exchange tank.Compressor is used to provide system
Heat energy in cold medium, condenser absorption refrigeration medium, the water transferred heat in the second heat exchange tank, in the second heat exchange tank
Water heated；The heat energy of water in first heat exchange tank is passed to refrigerant medium by the second evaporator, raises refrigerant
Temperature, so as to reduce the water temperature in the first heat exchange tank.So circulation, constantly realizes the heating to the water in the second heat exchange tank.
Further, described heating system includes being used for storing and export hot water hot-water cylinder, by the heat in hot-water cylinder
The 5th pump between water input tobacco roasting, heating system also includes the 4th pump for being used to extract out in the water in hot-water cylinder, described the
Four pumps are connected with hot-water cylinder and the second heat exchange tank by water pipe, and second heat exchange tank is provided with water inlet and delivery port, institute
State water inlet and delivery port and the circulatory system is constituted by water pipe and the hot-water cylinder；Described hot-water cylinder is dried by pipeline and tobacco
Bake interior second heat exchanger connection.
The heating system that the utility model is provided is by pipeline successively by between hot-water cylinder, the second heat exchange tank and tobacco roasting
It is tightly connected to form the circulatory system, the water in hot-water cylinder is flowed into the second heat exchange tank, is heated by condenser, after being heated
Water flow into hot-water cylinder in, then via water pipe import tobacco roasting between carry out heat supply.The utility model provide heating system with
Water is heat exchange medium, constantly be tobacco roasting between thermal source is provided.
Further, described temperature elevation system includes first heat exchanger, connects the first pressure of first heat exchanger respectively
Contracting machine, the first capillary, the first described compressor and the other end of the first capillary connect the first evaporator；Temperature elevation system is also
Cold water tank, including inlet channel, outlet conduit, the first pump are connected, inlet channel one end connects the first evaporator, other end connection
Cold water tank；First pump is on outlet conduit, and outlet conduit one end connects the bottom of cold water tank, and other end connection first is evaporated
Device；First heat exchanger connects the first compressor by the first pipeline；First described capillary one end is connected by second pipe
The first evaporator is connect, the other end of the first capillary connects first heat exchanger by the 3rd pipeline；The first described heat exchange
Device is in tobacco roasting.Described blower system includes the first blower fan, and the first blower fan blows to first heat exchanger, the second heat
Exchanger.
In the utility model, thermal source is first heat exchanger, and first heat exchanger effect is release heat, is so eliminated
The heating chamber of traditional tobacco flue-curing house, adds the space using flue-cured tobacco.
In the utility model, in the first pipeline is gases at high pressure, general 70 degree of temperature.In second pipe is low pressure gas
In state working medium, the 3rd pipeline is high-pressure gas-liquid mixed working fluid.
Compared with prior art, beneficial effect is：The utility model supplies a kind of tobacco flue-curing house, and heat utilization rate is high, a water outlet
Without going out fragrance；And fast and effectively the hot and humid gas tobacco roasting can be dehumidified, damp-heat can be recycled
The heat energy of body, and heat-exchange system is controllable, improves the efficiency of heat exchange；And heat-exchange system also includes being used to sense refrigeration system
System and the induction installation of heating system temperature, so setting according to circumstances can carry out heat exchange, and the speed that adjustment is exchanged in real time
Rate, improves the efficiency and validity of heat exchange.Heat-exchange system is provided with some assisted capillaries and induction installation simultaneously, so
Set and according to circumstances can carry out heat exchange, and the speed that adjustment is exchanged in real time, improve the efficiency and validity of heat exchange.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram.
Fig. 2 is the structural representation of heat-exchange system.
Embodiment
Accompanying drawing being given for example only property explanation, it is impossible to be interpreted as the limitation to this patent；It is attached in order to more preferably illustrate the present embodiment
Scheme some parts to have omission, zoom in or out, do not represent the size of actual product；To those skilled in the art,
Some known features and its explanation may be omitted and will be understood by accompanying drawing.Being given for example only property of position relationship described in accompanying drawing
Explanation, it is impossible to be interpreted as the limitation to this patent.
As shown in Fig. 1 to 2, a kind of tobacco flue-curing house, wherein, including dehumidified tobacco roasting dehumidification system, with removing
The refrigeration system of wet system connection, in addition to heating system, heat-exchange system, described heat-exchange system located at refrigeration system with
It is connected between heating system and respectively with refrigeration system, heating system；
Also include the blower system in tobacco roasting, and improving the temperature elevation system of temperature tobacco roasting；
Described heat-exchange system includes the second capillary 8, the second evaporator 9, the second compressor 7 and condenser 10,
Second capillary 8, the second evaporator 9, the compressor 7 of condenser 10 and second constitute closed circulation system by placed in series
System；
Some assisted capillaries 111 in parallel of second capillary 8, the parallel branch of the assisted capillary 111 is set
There is the control device 112 of the control working condition of assisted capillary 111, the heat-exchange system also includes being used to sense refrigeration system
With the induction installation of heating system temperature, the induction installation is electrically connected with control device 112.
Such as the left-hand component in Fig. 1, dehumidification system include the 3rd heat exchanger 13 for air-flow heat exchange and air inlet,
Dehydrating unit 12 and the second blower fan 11 for the air-flow after dehumidifying to be inputted between tobacco roasting；3rd heat exchanger 13
It is described to remove provided with the second channel 102 passed through for the first passage 101 and dry and cold air-flow of damp and hot airflow or xeothermic air-flow
Wet device 12 is provided with the third channel 103 for the cold water flow for being used for being dehumidified to damp-heat stream and for damp and hot airflow
Fourth lane 104, the first passage 101 is connected with fourth lane 104, the air-flow and second channel of the first passage 101
The 102 mutual heat exchange of air-flow；3rd heat exchanger 13, which is provided with, is used for the second entrance 107 that the damp and hot air-flow of baking room is flowed into；Institute
The connection refrigeration system of dehydrating unit 12 stated.
Wherein, the temperature range of the damp and hot air-flow is 60 °C ~ 70 °C.Dried it should be noted that this temperature is tobacco
The temperature of hot and humid gas between roasting, but the temperature difference between some tobacco roastings is understandable, because itself and tobacco
The equipment and seal degree of baking room etc. are relevant.
In addition, the temperature of the cold water of the flowing of the third channel 103 is 5 °C ~ 7 °C.Preferably, the third channel
The temperature of the cold water of 103 flowing is 6 °C.It should be noted that this temperature is preferred, it is not uniquely to limit.
Wherein, the temperature of the dry and cold air-flow is 15 °C ~ 20 °C.This temperature is that damp and hot air-flow is dehumidified after device dehumidifying
Temperature, but this is preferred, is not limited.
In addition, the temperature of the xeothermic air-flow is 29 °C ~ 35 °C.It should be noted that by the 3rd heat exchanger 13, doing
The temperature of cold airflow gets a promotion, and improves temperature and is again introduced into baking room, had so both realized the cyclic code of energy, and it also avoid
Fragrance overflows, and realizes recycling for energy and gas.
Further, refrigeration system includes the cold water tank 17 with the dehydrating unit 12 formation water circulation, the cold water tank
17 provided with the first delivery port 301 and the first water inlet 302 being connected with dehydrating unit；First water inlet 302 and first goes out
The mouth of a river 301 is arranged on the top of cold water tank 17；
The third channel 103 is provided with the first input port 105 and the first delivery outlet 106, first input port 105 and the
One delivery outlet 106 is connected with the water inlet 302 of the first delivery port 301 and first respectively, so that the cold water tank 17 and dehumidifying
The formation water circulation system of device 12；The junction of the delivery port 301 of first input port 105 and first is provided with the 3rd pump 16；Institute
The connection heat-exchange system of cold water tank 17 stated.
Further, the cold water tank 17 is provided with the display device for being used for showing the water level of cold water tank 17；The dehumidifying system
System is installed on tobacco flue-curing house by demountable structure.Cold water tank 17 described in the present embodiment, which is provided with, to be used to show the water level of cold water tank 17
Display device, the dehumidification system is installed on tobacco flue-curing house by demountable structure, and it is for the ease of observation cold water so to set
The water level of tank 17, so that cold water tank 17 can preferably provide the low-temperature receiver of dehydrating unit, and be easy to the maintenance of dehumidification system with
And install and use.
On the one hand, cold water tank 17 carries out water circulation with dehydrating unit 12, directly provides low-temperature receiver, the opposing party for dehydrating unit 12
Face, the heat exchange tank 206 of cold water tank 17 and first carries out water circulation, and the water of cold water tank 17 can be entered at the first heat exchange tank 206
One step is cooled down, and the water after cooling is being neutralized with the water after dehumidifying heat absorption so that the water in cold water tank 17 is able to maintain that certain
Temperature range.
Heat-exchange system includes the second capillary 8, the second evaporator 9, the second compressor 7 and condenser 10, described the
Two capillaries 8, the second evaporator 9, the compressor 7 of condenser 10 and second constitute closed cycle system by placed in series；
The heat-exchange system also includes the second heat exchange tank 205 for accommodating condenser 10 and evaporated for accommodating second
First heat exchange tank 206 of device 9；First heat exchange tank 206 is provided with the second input port 306 and the second delivery outlet 307, second input
The second water inlet of the delivery outlet 307 of mouth 306 and second respectively with the second delivery port 303 and the sidepiece of cold water tank 17 of the bottom of cold water tank 17
Mouth 304 is connected, so that the heat exchange tank 206 of the cold water tank 17 and first formation water circulation system；Second delivery port 303 and second defeated
The junction of entrance 306 is provided with the second pump 15.
Heating system is dried including the hot-water cylinder 20 for storing and exporting hot water, by the hot water input tobacco in hot-water cylinder 20
The 5th pump 19 between roasting, heating system also includes the 4th pump 18 for being used to extract out in the water in hot-water cylinder 20, the 4th pump 18
It is connected with the heat exchange tank 205 of hot-water cylinder 20 and second by water pipe, second heat exchange tank 205 is provided with water inlet 207 and gone out
The mouth of a river 208, the water inlet 207 and delivery port 208 constitute the circulatory system by water pipe and the hot-water cylinder 20；Described hot water
Tank 20 is connected by the second heat exchanger 6 in pipeline and tobacco roasting.
The heat-exchange system that the utility model is provided is sequentially connected the second capillary 8 by pipeline, the second evaporator 9, cold
The compressor 7 of condenser 10 and second forms the closed circulatory system, and the condenser 10 is immersed in the water of the second heat exchange tank 205,
Second evaporator 9 is immersed in the water of the first heat exchange tank 206.Second compressor 7 is used to provide refrigerant, condenser 10
Heat energy in absorption refrigeration medium, the water transferred heat in the second heat exchange tank 205 enters to the water in the second heat exchange tank 205
Row heating；The heat energy of water in first heat exchange tank 206 is passed to refrigerant medium by the second evaporator 9, rise refrigerant
Temperature, so as to reduce the water temperature in the first heat exchange tank 206.So circulation, constantly realizes adding to the water in the second heat exchange tank 205
Heat.
Set that the 4th pump 18 can be rapidly and efficiently the water in hot-water cylinder is pumped into the second heat exchange tank is heated, to carry
The heating efficiency of high heating system.The heating system that the utility model is provided successively is exchanged heat hot-water cylinder 20, second by pipeline
It is tightly connected to form the circulatory system between tank 205 and tobacco roasting, the water in hot-water cylinder 20 is flowed into the second heat exchange tank 205, leads to
Cross condenser 10 to be heated, the water after being heated is flowed into hot-water cylinder 20, then supplied between water pipe importing tobacco roasting
Heat.The utility model provide heating system using water as heat exchange medium, constantly be tobacco roasting between thermal source is provided.Second heat is handed over
Parallel operation 6 distributes heat.
Temperature elevation system includes first heat exchanger 2, respectively the first compressor 3 of connection first heat exchanger 2, the first capillary
Pipe 5, the first described compressor 3 and the other end of the first capillary 5 connect the first evaporator 4；Temperature elevation system is also connected with cold water
Tank 17, including inlet channel 409, outlet conduit 410, the first pump 14, one end of inlet channel 409 connect the first evaporator 4, another
End connection cold water tank 17；First pump 14 is on outlet conduit 410, and the one end of outlet conduit 410 connects the bottom of cold water tank 17, separately
One end connects the first evaporator 4；First heat exchanger 2 connects the first compressor 3 by the first pipeline 406；Described first mao
The one end of tubule 5 connects the first evaporator 4 by second pipe 407, and the other end of the first capillary 5 is connected by the 3rd pipeline 408
Connect first heat exchanger 2；Described first heat exchanger 2 is in tobacco roasting.
In the present embodiment, thermal source is first heat exchanger 2, and the effect of first heat exchanger 2 is release heat, is so eliminated
The heating chamber of traditional tobacco flue-curing house, adds the space using flue-cured tobacco.
In the utility model, in the first pipeline 406 is gases at high pressure, general 70 degree of temperature.In second pipe 407 is
In low-pressure gaseous working medium, the 3rd pipeline 408 is high-pressure gas-liquid mixed working fluid.
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 (9)
1. a kind of tobacco flue-curing house, it is characterised in that including be sequentially connected with dehumidification system, refrigeration system, in addition to heating system, heat
Exchange system, described heat-exchange system be located between refrigeration system and heating system and respectively with refrigeration system, heating system
Connection；
Also include the blower system in tobacco roasting, and improving the temperature elevation system of temperature tobacco roasting；
Described heat-exchange system includes the second capillary（8）, the second evaporator（9）, the second compressor（7）And condenser
（10）, second capillary（8）, the second evaporator（9）, condenser（10）With the second compressor（7）Pass through placed in series structure
Into closed cycle system；
Second capillary（8）Some assisted capillaries in parallel（111）, the assisted capillary（111）Parallel branch set
It is equipped with control assisted capillary（111）The control device of working condition（112）, the heat-exchange system is also including being used to sense system
Cooling system and the induction installation of heating system temperature, the induction installation and control device（112）Electrical connection.
2. a kind of tobacco flue-curing house according to claim 1, it is characterised in that：Described dehumidification system includes being used for air-flow heat friendship
Change and air inlet the 3rd heat exchanger（13）, dehydrating unit（12）And for the air-flow after dehumidifying to be inputted between tobacco roasting
The second blower fan（11）；3rd heat exchanger（13）Provided with the first passage for damp and hot airflow（101）With it is dry and cold
The second channel that air-flow or xeothermic air-flow pass through（102）, the dehydrating unit（12）Provided with for being dehumidified to damp-heat stream
Cold water flow third channel（103）With the fourth lane for damp and hot airflow（104）, the first passage（101）
With fourth lane（104）Connection, the first passage（101）Air-flow and second channel（102）The mutual heat exchange of air-flow；The
Three heat exchangers（13）Provided with the second entrance flowed into for the damp and hot air-flow of baking room（107）；Described dehydrating unit（12）Even
Connect refrigeration system.
3. a kind of tobacco flue-curing house according to claim 2, it is characterised in that：Described refrigeration system includes filling with the dehumidifying
Put（12）Form the cold water tank of water circulation（17）, the cold water tank（17）Provided with the first delivery port being connected with dehydrating unit
（301）With the first water inlet（302）；First water inlet（302）With the first delivery port（301）It is arranged on cold water tank（17）'s
Top；
The third channel（103）Provided with the first input port（105）With the first delivery outlet（106）, first input port（105）
With the first delivery outlet（106）Respectively with first delivery port（301）With the first water inlet（302）Connection, so that the cold water
Tank（17）With dehydrating unit（12）Form water circulation system；First input port（105）With the first delivery port（301）Connection
Place is provided with the 3rd pump（16）；Described cold water tank（17）Connect heat-exchange system.
4. a kind of tobacco flue-curing house according to claim 3, it is characterised in that：The cold water tank（17）Being provided with is used to show cold
Water pot（17）The display device of water level.
5. a kind of tobacco flue-curing house according to any one of Claims 1-4, it is characterised in that：The dehumidification system passes through removable
Unload structure and be installed on tobacco flue-curing house.
6. a kind of tobacco flue-curing house according to claim 4, it is characterised in that：The heat-exchange system also includes being used to accommodate
Condenser（10）The second heat exchange tank（205）With for accommodating the second evaporator（9）The first heat exchange tank（206）；First heat exchange
Tank（206）Provided with the second input port（306）With the second delivery outlet（307）, second input port（306）With the second delivery outlet
（307）Respectively with cold water tank（17）Second delivery port of bottom（303）And cold water tank（17）Second water inlet of sidepiece（304）Even
Connect, so that the cold water tank（17）With the first heat exchange tank（206）Form water circulation system；Second delivery port（303）It is defeated with second
Entrance（306）Junction be provided with the second pump（15）.
7. a kind of tobacco flue-curing house according to claim 6, it is characterised in that：Described heating system includes being used to store and defeated
Go out the hot-water cylinder of hot water（20）, by hot-water cylinder（20）In hot water input tobacco roasting between the 5th pump（19）, heating system is also
Including for by hot-water cylinder（20）In water extract out the 4th pump（18）, the 4th pump（18）With hot-water cylinder（20）And second
Heat exchange tank（205）Connected by water pipe, second heat exchange tank（205）It is provided with water inlet（207）And delivery port（208）, institute
State water inlet（207）And delivery port（208）Pass through water pipe and the hot-water cylinder（20）Constitute the circulatory system；Described hot-water cylinder
（20）Pass through the second heat exchanger in pipeline and tobacco roasting（6）Connection.
8. a kind of tobacco flue-curing house according to claim 7, it is characterised in that：Described temperature elevation system includes first heat exchanger
（2）, connect first heat exchanger respectively（2）The first compressor（3）, the first capillary（5）, described the first compressor（3）
With the first capillary（5）The other end connect the first evaporator（4）；Temperature elevation system is also connected with cold water tank（17）, including water inlet pipe
Road（409）, outlet conduit（410）, the first pump（14）, inlet channel（409）One end connects the first evaporator（4）, other end company
Connect cold water tank（17）；First pump（14）Located at outlet conduit（410）On, outlet conduit（410）One end connects cold water tank（17）'s
Bottom, the other end connects the first evaporator（4）；First heat exchanger（2）Pass through the first pipeline（406）Connect the first compressor
（3）；The first described capillary（5）One end passes through second pipe（407）Connect the first evaporator（4）, the first capillary（5）'s
The other end passes through the 3rd pipeline（408）Connect first heat exchanger（2）；Described first heat exchanger（2）Located at tobacco roasting
In.
9. a kind of tobacco flue-curing house according to claim 8, it is characterised in that：Described blower system includes the first blower fan（1）,
First blower fan（1）Blow to first heat exchanger（2）, second heat exchanger（6）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378465.1U CN206443182U (en) | 2016-12-15 | 2016-12-15 | A kind of tobacco flue-curing house |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621378465.1U CN206443182U (en) | 2016-12-15 | 2016-12-15 | A kind of tobacco flue-curing house |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206443182U true CN206443182U (en) | 2017-08-29 |
Family
ID=59672849
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621378465.1U Expired - Fee Related CN206443182U (en) | 2016-12-15 | 2016-12-15 | A kind of tobacco flue-curing house |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206443182U (en) |
-
2016
- 2016-12-15 CN CN201621378465.1U patent/CN206443182U/en not_active Expired - Fee Related
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