CN206443173U - A kind of energy saving flue-cured tobacco-room - Google Patents
A kind of energy saving flue-cured tobacco-room Download PDFInfo
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- CN206443173U CN206443173U CN201621375068.9U CN201621375068U CN206443173U CN 206443173 U CN206443173 U CN 206443173U CN 201621375068 U CN201621375068 U CN 201621375068U CN 206443173 U CN206443173 U CN 206443173U
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Abstract
The utility model is related to the technical field of flue-cured tobacco, more particularly, to a kind of energy saving flue-cured tobacco-room.A kind of energy saving flue-cured tobacco-room, wherein, the refrigeration system being connected including the dehumidification system being dehumidified tobacco roasting, with dehumidification system, also include 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.The heating chamber of traditional tobacco flue-curing house is eliminated, the space using flue-cured tobacco is added, heat utilization rate is high.
Description
Technical field
The utility model is related to the technical field of flue-cured tobacco, more particularly, to a kind of energy saving flue-cured tobacco-room.
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.
The content of the invention
The utility model is to overcome at least one defect described in above-mentioned prior art there is provided a kind of energy saving flue-cured tobacco-room, hot
Energy utilization rate is high, and a water outlet is without going out fragrance；And fast and effectively the hot and humid gas tobacco roasting can be dehumidified,
The heat energy of hot and humid gas can be recycled, and system architecture is simple, it is easy to use.
In order to solve the above technical problems, the technical solution adopted in the utility model is：A kind of energy saving flue-cured tobacco-room, wherein, bag
Include and the dehumidification system dehumidified tobacco roasting, the refrigeration system being connected with dehumidification system, in addition to heating system, heat are handed over
System is changed, described heat-exchange system is located between refrigeration system and heating system and connected respectively with refrigeration system, heating system
Connect；
Also include the blower system in tobacco roasting.
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, 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.
In the utility model, thermal source is second heat exchanger, and second 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.
Compared with prior art, beneficial effect is：The utility model passes through the 3rd for air-flow heat exchange and air inlet
Heat exchanger, dehydrating unit and for by after dehumidifying air-flow input tobacco roasting between blower fan setting so that dehumidifying system
System utilizes heat transfer, and the heat of hot and humid gas is recycled in the 3rd heat exchanger, and using dehydrating unit to hot and humid gas
Dehumidified, the gas after dehumidification system is handled using blower fan is re-circulated between tobacco roasting, realizes energy gentle
The circulation of body, it is to avoid energy dissipation and fragrance overflow.And the dehumidification system between tobacco roasting of the present utility model is simple in construction,
It is easy to use and cost is low.And the application process of the system both facilitated, and environmentally friendly, recycling for heat is realized, and keep away
Fragrance spilling is exempted from.
The utility model thermal source is second heat exchanger, and the effect of second heat exchanger is release heat, is so eliminated
The heating chamber of traditional tobacco flue-curing house, adds the space using flue-cured tobacco, and heat utilization rate is high.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram.
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 figure 1, a kind of energy saving flue-cured tobacco-room, 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.
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.
The step of dehumidifying is specially：
A. the damp-heat stream between tobacco roasting inputs the first passage 101 of the 3rd heat exchanger 13 by second entrance 107
In；
B. the damp-heat stream in first passage 101 is entered by feed channel in the fourth lane 104 of dehydrating unit 12；
C. the third channel 103 for being used for the cold water flow of dehumidifying carries out cool-down dehumidification to the damp-heat stream in fourth lane,
Removing the moisture in damp and hot air-flow makes it become dry and cold air-flow；
D. dry and cold air-flow is back to by feed channel in the second channel 102 of the 3rd heat exchanger 13；
E. the dry and cold air-flow of second channel 102 carries out heat exchange with cycling through the damp-heat stream of first passage 101, dry and cold
Air-flow is heated to form xeothermic air-flow；
F. xeothermic air-flow is inputted in the second blower fan 11 by feed channel, and xeothermic air-flow is inputted tobacco roasting by the second blower fan 11
Between.
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.
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.
In the present embodiment, thermal source is second heat exchanger 6, and the effect of second heat exchanger 6 is release heat, is so eliminated
The heating chamber of traditional tobacco flue-curing house, adds the space using flue-cured tobacco.
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 (6)
1. a kind of energy saving flue-cured tobacco-room, it is characterised in that including the dehumidification system and dehumidification system being dehumidified tobacco roasting
The refrigeration system of connection, in addition to heating system, heat-exchange system, described heat-exchange system is located at refrigeration system and heat supply system
It is connected between system and respectively with refrigeration system, heating system；
Also include the blower system in tobacco roasting.
2. a kind of energy saving flue-cured tobacco-room according to claim 1, it is characterised in that：Described dehumidification system includes being used for air-flow
Heat exchange and the 3rd heat exchanger of air inlet（13）, dehydrating unit（12）And for the air-flow input tobacco after dehumidifying to be dried
The second blower fan between roasting（11）；3rd heat exchanger（13）Provided with the first passage for damp and hot airflow（101）With
The second channel that dry and cold air-flow or xeothermic air-flow pass through（102）, the dehydrating unit（12）Provided with for being carried out to damp-heat stream
The third channel of the cold water flow of dehumidifying（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）Air-flow mutually heat hand over
Change；3rd heat exchanger（13）Provided with the second entrance flowed into for the damp and hot air-flow of baking room（107）；Described dehydrating unit
（12）Connect refrigeration system.
3. a kind of energy saving flue-cured tobacco-room according to claim 2, it is characterised in that：Described refrigeration system includes removing with described
Wet device（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 energy saving flue-cured tobacco-room according to claim 3, it is characterised in that：Described heat-exchange system includes second mao
Tubule（8）, the second evaporator（9）, the second compressor（7）And condenser（10）, second capillary（8）, second evaporation
Device（9）, condenser（10）With the second compressor（7）Closed cycle system is constituted by placed in series；
The heat-exchange system also includes being used to accommodate condenser（10）The second heat exchange tank（205）Evaporated with for accommodating second
Device（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）, institute
State the 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）Connection, so that the cold water tank（17）With the first heat exchange tank（206）Form water circulation
System；Second delivery port（303）With the second input port（306）Junction be provided with the second pump（15）.
5. a kind of energy saving flue-cured tobacco-room according to claim 4, it is characterised in that：Described heating system includes being used to store
And export the hot-water cylinder of hot water（20）, by hot-water cylinder（20）In hot water input tobacco roasting between the 5th pump（19）, heat supply system
System also includes being used for 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）, the 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.
6. a kind of energy saving flue-cured tobacco-room according to claim 5, it is characterised in that：Described blower system includes the first blower fan
（1）, the first blower fan（1）Blow to second heat exchanger（6）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621375068.9U CN206443173U (en) | 2016-12-15 | 2016-12-15 | A kind of energy saving flue-cured tobacco-room |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621375068.9U CN206443173U (en) | 2016-12-15 | 2016-12-15 | A kind of energy saving flue-cured tobacco-room |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206443173U true CN206443173U (en) | 2017-08-29 |
Family
ID=59673850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621375068.9U Expired - Fee Related CN206443173U (en) | 2016-12-15 | 2016-12-15 | A kind of energy saving flue-cured tobacco-room |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206443173U (en) |
-
2016
- 2016-12-15 CN CN201621375068.9U patent/CN206443173U/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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170829 Termination date: 20191215 |