CN206989605U - Integral type high temperature drying dehumidification machine - Google Patents
Integral type high temperature drying dehumidification machine Download PDFInfo
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- CN206989605U CN206989605U CN201720899918.3U CN201720899918U CN206989605U CN 206989605 U CN206989605 U CN 206989605U CN 201720899918 U CN201720899918 U CN 201720899918U CN 206989605 U CN206989605 U CN 206989605U
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Abstract
Integral type high temperature drying dehumidification machine,Including drying chamber,Drying chamber is connected with circulation air path and air inlet duct,Dehydrating unit is installed between circulation air path and air inlet duct,At least one heat exchanger is installed in the dehydrating unit,The first air-valve is installed between the first air inlet and circulation air path in heat exchanger,First gas outlet connects with the first air intake of evaporator and the second air intake of condenser respectively,The 3rd air-valve is installed between first gas outlet and the first air intake of evaporator,The 4th air-valve is installed between first gas outlet and the second air intake of condenser,Second air inlet connects with the first air port,Be provided with first air port can rotating the first blower fan,Second gas outlet connects with the second air intake of condenser,The second air-valve is installed between second gas outlet and the second air intake of condenser,During heat exchange being carried out by the hot-air in cold air inside and baking zone,Dehumidification by condensation is carried out to the vapor in baking zone.
Description
Technical field
It the utility model is related to drying unit field, especially integral type high temperature drying dehumidification machine.
Background technology
High-temperature dryer is widely used in every field, including agricultural product, chemical products, hardware products etc., has the energy
The advantages that consumption is few, and environmental pollution is small, applied widely, baking zone is sent hot blast into by heat pump drying dehumidifier, to drying
Indoor product carries out drying dehumidification, completes the hot blast after drying and is become moist through due to absorbing the moisture of product, then existing
Hot wet air heating is directly discharged outdoor by wet-emitting blower, covers fresh sky by modern heat pump drying dehumidifier in dehumidification process
Gas, the thermal loss so to dehumidify is very big, while the quality of the fresh air covered is uncontrollable, and portioned product is being dried
During, the penetrating odor or toxic odor of product are mingled in Hot wet air heating, directly exclude outdoor easily pollution environment, shadow
The health problem for arriving people is rung, such as using the method for evaporator sealing dehumidifying, evaporator, which works long hours, increases drying dehumidification machine
Energy consumption, improve production cost.
Utility model content
The purpose of this utility model is solve above-mentioned the deficiencies in the prior art, and provides a kind of simple and reasonable one
Formula high temperature drying dehumidification machine.
Technical scheme is used by the utility model solves its technical problem：
Integral type high temperature drying dehumidification machine, including drying chamber, drying chamber are connected with circulation air path and air inlet duct, circulation air path
Dehydrating unit is installed between air inlet duct, dehydrating unit offers the first air port and the second air port, pacified in dehydrating unit respectively
Equipped with evaporator and condenser, evaporator is disposed adjacent with the second air port, and condenser is disposed adjacent with air inlet duct, the dehumidifying dress
At least one heat exchanger is installed in putting, the first pipeline and second pipe being staggered, the first pipe are included in heat exchanger
Road both ends respectively constitute the first air inlet and the first gas outlet, and second pipe both ends respectively constitute the second air inlet and the second outlet
Mouthful, the first air inlet is connected with circulation air path, and the first air-valve, the first gas outlet are provided between the first air inlet and circulation air path
Connected respectively with the first air intake of evaporator and the second air intake of condenser, the first air intake of the first gas outlet and evaporator
3rd air-valve is installed between end, the 4th air-valve is installed between the first gas outlet and the second air intake of condenser, second enters
Gas port connects with the first air port, be provided with the first air port can rotating the first blower fan, the of the second gas outlet and condenser
Two air intakes connect, and the second air-valve are provided between the second gas outlet and the second air intake of condenser, cold air inside is with drying
During hot-air in dry chamber carries out heat exchange, dehumidification by condensation is carried out to the vapor in drying chamber, passes through the first blower fan
Rotating is realized, dehumidifier is realized dehumidifying, hydrofuge and defrost process.
Preferential, heat exchanger and lower heat exchanger, upper heat exchanger and lower heat exchanger are installed in dehydrating unit
Two first pipeline communications, the second air inlet of upper heat exchanger connects with the first air port, the second gas outlet of lower heat exchanger
Connected with the first air intake, the second gas outlet of upper heat exchanger and the second air inlet of lower heat exchanger are connected by interface channel
It is logical, heat exchange cold efficiency is improved, it is simple in construction.
Preferential, the second air-valve is installed on the interface channel.
Preferential, the air inlet duct is provided with the second blower fan, and the second blower fan improves wind speed and entered in drying chamber.
Preferential, the 3rd blower fan is installed, the 3rd blower fan can improve the speed of air flow on the 3rd air-valve.
Preferential, the first outlet air end of the evaporator connects with the second air port.
Preferential, the second air intake of the condenser connects with air inlet duct.
The beneficial effects of the utility model are：
Integral type high temperature drying dehumidification machine of the present utility model, its is simple and reasonable for structure, passes through cold air inside and drying
During hot-air in area carries out heat exchange, dehumidification by condensation is carried out to the vapor in baking zone, in the baking zone of closing
The process of dehumidifying is completed, avoids the penetrating odor of product or toxic odor from being mingled in Hot wet air heating, directly excludes outdoor appearance
Easily pollution environment, has influence on the health problem of people, while reduces the energy consumption of dehumidifier, accomplishes energy-saving and emission-reduction, and pass through wind
Dehumidifying, hydrofuge and defrost process are realized in the rotating of machine.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is partial structural diagram of the present utility model.
Fig. 3 is dehumidifying schematic flow sheet of the present utility model.
Fig. 4 is hydrofuge schematic flow sheet of the present utility model.
Fig. 5 is defrost schematic flow sheet of the present utility model.
Embodiment
The utility model is further illustrated with reference to the accompanying drawings and examples：
As shown in Figure 1 to Figure 2：Integral type high temperature drying dehumidification machine, including drying chamber 1, drying chamber 1 are connected with circulation air path
2 and air inlet duct 3, dehydrating unit 4 is installed, dehydrating unit 4 offers the first air port 5 respectively between circulation air path 2 and air inlet duct 3
With the second air port 6, evaporator 7 and condenser 8 are installed in dehydrating unit 4, evaporator 7 is disposed adjacent with the second air port 6, condensation
Device 8 is disposed adjacent with air inlet duct 3, and at least one heat exchanger 9 is provided with the dehydrating unit 4, includes handing in heat exchanger 9
The first pipeline 10 and second pipe 11 that mistake is set, the both ends of the first pipeline 10 respectively constitute the first air inlet 12 and the first gas outlet
13, the both ends of second pipe 11 respectively constitute the second air inlet 14 and the second gas outlet 15, and the first air inlet 12 connects with circulation air path 2
It is logical, the first air-valve 16 is installed between first air inlet 12 and circulation air path 2, the first gas outlet 13 respectively with evaporator 7 the
One air intake 701 connects with the second air intake 801 of condenser 8, the first gas outlet 13 and the first air intake 701 of evaporator 7
Between the 3rd air-valve 17 is installed, the 4th air-valve is installed between the first gas outlet 13 and the second air intake 801 of condenser 8
18, the second air inlet 14 connects with the first air port 5, be provided with the first air port 5 can rotating the first blower fan 19, the second outlet
Mouth 13 connects with the second air intake 801 of condenser 8, is installed between the second gas outlet 15 and the second air intake 801 of condenser 8
There is the second air-valve 20, during cold air inside carries out heat exchange with the hot-air in drying chamber 1, to the water in drying chamber 1
Steam carries out dehumidification by condensation, and rotating is realized by the first blower fan 19, dehumidifier is realized dehumidifying, hydrofuge and defrost process.
Heat exchanger 9a and lower heat exchanger 9b are installed, upper heat exchanger 9a and lower heat are handed in the dehydrating unit 4
Parallel operation 9b two first pipelines 10 connect, and upper heat exchanger 4a the second air inlet 14 connects with the first air port 5, lower heat exchanger
9b the second gas outlet 15 connects with the first air intake 701, upper heat exchanger 9a the second gas outlet 15 and lower heat exchanger 9b
The second air inlet 14 connected by interface channel 21, improve heat exchange cold efficiency, it is simple in construction.
Second air-valve 20 is installed on the interface channel 21.
The air inlet duct 3 is provided with the second blower fan 22, and the second blower fan 22 improves wind speed and entered in drying chamber 1.
3rd blower fan 23 is installed, the 3rd blower fan 23 can improve the speed of air flow on the 3rd air-valve 17.
First outlet air end 702 of the evaporator 7 connects with the second air port 6.
Second air intake 802 of the condenser 8 connects with air inlet duct 3.
Dehumidifying flow of the present utility model is as shown in Figure 3：
First blower fan 19 rotates forward, and the first air-valve opens 16, and the second air-valve 20 is closed, and the 3rd air-valve 17 is closed, and the 4th
Air-valve 18 is opened, and outdoor air enters dehydrating unit 4 after reducing temperature through evaporator 7 from the second air port 6, then through overheat
The second pipe 11 of exchanger 9, finally discharged from the first air port 5, now, the part hot-air in drying chamber 1 passes through circulated air
Road 2 is entered in dehydrating unit 4 by the first air-valve 16, first pipeline 10 of the hot-air through over-heat-exchanger 9, and by second
The cold air of pipeline 11 carries out heat exchange, and in heat exchanging process, the damp-heat air in hot-air is condensed, and realizes dehumidifying
Process, the hot-air after cooling are finally recycled in drying chamber 1 by the 4th air-valve 18, condenser 8, air inlet duct 3.
Hydrofuge flow of the present utility model is as shown in Figure 4：
First blower fan 19 is rotated backward, and the first air-valve 16 is opened, and the second air-valve 20 is opened, and the 3rd air-valve 17 is opened, and the 4th
Air-valve 18 is closed, and outdoor cold air enters dehydrating unit 4 from the first air port 5, then the second pipe 11 through over-heat-exchanger,
Part cold air enters the second air intake 801 of condenser 8 then into drying chamber 1 by the second air-valve 20, in addition
Part cold air is finally discharged by the 3rd air-valve 17 and evaporator 7 from the second air port 6, and now, the part heat in drying chamber 1 is empty
Gas is entered in dehydrating unit 4 by circulation air path 2 by the first air-valve 16, first pipeline of the hot-air through over-heat-exchanger 9
10, with carrying out heat exchange by the cold air of second pipe 11, in heat exchanging process, the damp-heat air in hot-air is carried out
Globule discharge outdoor is condensed into, part damp-heat air discharges outdoor by the 3rd air-valve 17, the air port 6 of evaporator 7 and second, real
Show hydrofuge process, the heat contained in the damp-heat air of part during evaporator 6 by being absorbed and used again.
Defrost flow of the present utility model is as shown in Figure 5：
First blower fan 19 is rotated backward, and the first air-valve 16 is opened, and the second air-valve 20 is closed, and the 3rd air-valve 17 is closed, and the 4th
Air-valve 18 is opened, and outdoor cold air enters dehydrating unit 4 from the first air port 5, the second pipe then through over-heat-exchanger 9
11, cold air is finally discharged by the 3rd air-valve 17 and evaporator 7 from the second air port 6, and now, the part heat in drying chamber 1 is empty
Gas is entered in dehydrating unit 4 by circulation air path 2 by the first air-valve 16, first pipeline of the hot-air through over-heat-exchanger 9
10, with carrying out heat exchange by the cold air of second pipe 11, in heat exchanging process, the damp-heat air in hot-air is carried out
Condensation, realizes dehumidification process, and the hot-air after cooling is finally recycled to drying by the 4th air-valve 18, condenser 8, air inlet duct 3
In room 1, the air in the second pipe 11 to be heated up after heat absorption, during evaporator 7 is blowed to by the 3rd air-valve 17, air
In heat the frost on evaporator 7 is dissolved, make dehumidifier in dehumidification process while realize defrost process.
It should be noted that preferably implementation of the present utility model is given in specification of the present utility model and its accompanying drawing
Example, still, the utility model can be realized by many different forms, however it is not limited to the implementation described by this specification
Example, these embodiments are not as the extra limitation to the utility model content, there is provided the purpose of these embodiments is made to this reality
With the understanding more thorough and comprehensive of new disclosure.Also, above-mentioned each technical characteristic continues to be mutually combined, formed not upper
The various embodiments that face is enumerated, it is accordingly to be regarded as the scope of the utility model specification record；Further, to ordinary skill
For personnel, it can according to the above description be improved or be converted, and all these modifications and variations should all belong to this practicality newly
The protection domain of type appended claims.
Claims (7)
1. integral type high temperature drying dehumidification machine, including drying chamber（1）, drying chamber（1）It is connected with circulation air path（2）And air inlet duct
（3）, circulation air path（2）And air inlet duct（3）Between dehydrating unit is installed（4）, dehydrating unit（4）The first air port is offered respectively
（5）With the second air port（6）, dehydrating unit（4）Evaporator is inside installed（7）And condenser（8）, evaporator（7）With the second air port
（6）It is disposed adjacent, condenser（8）With air inlet duct（3）It is disposed adjacent, its feature is being：The dehydrating unit（4）Inside it is provided with
At least one heat exchanger（9）, heat exchanger（9）Interior the first pipeline including being staggered（10）And second pipe（11）, the
One pipeline（10）Both ends respectively constitute the first air inlet（12）With the first gas outlet（13）, second pipe（11）Both ends respectively constitute
Second air inlet（14）With the second gas outlet（15）, the first air inlet（12）With circulation air path（2）Connection, the first air inlet（12）
With circulation air path（2）Between the first air-valve is installed（16）, the first gas outlet（13）Respectively with evaporator（7）The first air intake
（701）And condenser（8）The second air intake（801）Connection, the first gas outlet（13）With evaporator（7）The first air intake
（701）Between the 3rd air-valve is installed（17）, the first gas outlet（13）With condenser（8）The second air intake（801）Between pacify
Equipped with the 4th air-valve（18）, the second air inlet（14）With the first air port（5）Connection, the first air port（5）On be provided with can rotating
The first blower fan（19）, the second gas outlet（13）With condenser（8）The second air intake（801）Connection, the second gas outlet（15）
With condenser（8）The second air intake（801）Between the second air-valve is installed（20）.
2. integral type high temperature drying dehumidification machine according to claim 1, it is characterised in that：The dehydrating unit（4）Interior installation
There is upper heat exchanger（9a）With lower heat exchanger（9b）, upper heat exchanger（9a）With lower heat exchanger（9b）Two first pipelines
（10）Connection, upper heat exchanger（9a）The second air inlet（14）With the first air port（5）Connection, lower heat exchanger（9b）Second
Gas outlet（15）With the first air intake（701）Connection, upper heat exchanger（9a）The second gas outlet（15）With lower heat exchanger
（9b）The second air inlet（14）Pass through interface channel（21）Connection.
3. integral type high temperature drying dehumidification machine according to claim 2, it is characterised in that：The interface channel（21）Upper installation
There is the second air-valve（20）.
4. integral type high temperature drying dehumidification machine according to claim 1, it is characterised in that：The air inlet duct（3）It is provided with
Two blower fans（22）.
5. integral type high temperature drying dehumidification machine according to claim 1, it is characterised in that：3rd air-valve（17）Upper installation
There is the 3rd blower fan（23）.
6. integral type high temperature drying dehumidification machine according to claim 1, it is characterised in that：The evaporator（7）First go out
Wind end（702）With the second air port（6）Connection.
7. integral type high temperature drying dehumidification machine according to claim 1, it is characterised in that：The condenser（8）Second enter
Wind end（802）With air inlet duct（3）Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720899918.3U CN206989605U (en) | 2017-07-24 | 2017-07-24 | Integral type high temperature drying dehumidification machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720899918.3U CN206989605U (en) | 2017-07-24 | 2017-07-24 | Integral type high temperature drying dehumidification machine |
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| Publication Number | Publication Date |
|---|---|
| CN206989605U true CN206989605U (en) | 2018-02-09 |
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ID=61416931
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720899918.3U Active CN206989605U (en) | 2017-07-24 | 2017-07-24 | Integral type high temperature drying dehumidification machine |
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| CN (1) | CN206989605U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107238263A (en) * | 2017-07-24 | 2017-10-10 | 广东华天成新能源科技股份有限公司 | A kind of integral type high temperature drying dehumidification machine |
| CN108800898A (en) * | 2018-05-24 | 2018-11-13 | 浙江理工大学 | A kind of heat pump boiling drier device |
| CN108800770A (en) * | 2018-06-21 | 2018-11-13 | 广州能之原科技股份有限公司 | A kind of heat pump drying room |
-
2017
- 2017-07-24 CN CN201720899918.3U patent/CN206989605U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107238263A (en) * | 2017-07-24 | 2017-10-10 | 广东华天成新能源科技股份有限公司 | A kind of integral type high temperature drying dehumidification machine |
| CN107238263B (en) * | 2017-07-24 | 2024-02-20 | 广东华天成新能源科技股份有限公司 | Integrated high-temperature drying dehumidifier |
| CN108800898A (en) * | 2018-05-24 | 2018-11-13 | 浙江理工大学 | A kind of heat pump boiling drier device |
| CN108800770A (en) * | 2018-06-21 | 2018-11-13 | 广州能之原科技股份有限公司 | A kind of heat pump drying room |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 528308 Guangdong Province, Foshan city Shunde District Lunjiao Street office Yongfeng village two Industrial Zone No. 34 south of Patentee after: GUANGDONG HUATIANCHENG NEW ENERGY TECHNOLOGY CO., LTD. Address before: 528300 Guangdong province Foshan city Shunde District Daliang Street Chang Road No. 11 Patentee before: GUANGDONG HUATIANCHENG NEW ENERGY TECHNOLOGY CO., LTD. |