CN105605911A - Drying machine - Google Patents
Drying machine Download PDFInfo
- Publication number
- CN105605911A CN105605911A CN201610183397.1A CN201610183397A CN105605911A CN 105605911 A CN105605911 A CN 105605911A CN 201610183397 A CN201610183397 A CN 201610183397A CN 105605911 A CN105605911 A CN 105605911A
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- China
- Prior art keywords
- heat pipe
- air
- condenser
- evaporimeter
- box
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/086—Humidity by condensing the moisture in the drying medium, which may be recycled, e.g. using a heat pump cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/005—Compression machines, plants or systems with non-reversible cycle of the single unit type
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to a drying machine. The drying machine comprises a drying box and a dehumidifier butted with the drying box, wherein the dehumidifier comprises a dehumidification box body, a heat pipe, a refrigeration system and a blowing fan, wherein the dehumidification box body is provided with an air inlet and an air outlet which respectively communicate with the drying box; the lower part of the heat pipe forms a heat pipe evaporation section; the upper part of the heat pipe forms a heat pipe condensation section; the refrigeration system comprises an evaporator and a condenser; the blowing fan is arranged in the dehumidification box body in the position adjacent to the air outlet; air in the drying box enters the dehumidification box body via the air inlet, and sequentially flows through the heat pipe evaporation section, evaporator, heat pipe condensation section and condenser to the air outlet; and the blowing fan is used for sending the air flowing to the air outlet into the drying box. The dehumidifier is adopted to perform ventilation and dehumidification on the air in the drying box without shutdown, so that the parts can be dried only by heating the drying box to 50 DEG C. The drying machine has the advantages of favorable drying effect, power saving and higher work efficiency.
Description
Technical field
The present invention relates to a kind of drying plant.
Background technology
At present, in industrial production, often need to carry out fast dewatering oven dry to some parts. Existing conventional drying plant is high temperature oven, and this high temperature oven is with electrical heating, air heat to 90 DEG C high temperature to be come parts to dry. Because this high temperature oven can not dehumidify, the very high and airborne moisture of air humidity after repeatedly using in high temperature oven also cannot be discharged baking oven, makes the drying effect of baking oven very poor. In order to ensure the drying effect of baking oven, need timing shutdown to take a breath to dehumidify and then could continue use, this greatly reduces again the operating efficiency of high temperature oven, causes very large puzzlement to the oven dry of parts.
Summary of the invention
The technical problem to be solved in the present invention is to provide high, the energy-conservation dryer of a kind of drying efficiency.
In order to solve the problems of the technologies described above, a kind of technical scheme that the present invention adopts is: the dehydrating unit that a kind of dryer comprises drying baker and docks with drying baker. described dehydrating unit can be removed contained moisture in the interior air of drying baker, described dehydrating unit comprises dehumidifying casing, with the heat pipe being arranged in dehumidifying casing, refrigeration system and pressure fan, on described dehumidifying casing, offer the air intlet and the air outlet slit that are communicated with drying baker respectively, in described dehumidifying casing, form circulation of air air channel from air intlet to air outlet slit, described heat pipe is erected in dehumidifying casing, heat pipe evaporator section is formed at the bottom of described heat pipe, heat pipe condenser section is formed at the top of described heat pipe, described refrigeration system comprises the evaporimeter that is arranged on heat pipe evaporator section rear portion and the condenser that is arranged on heat pipe condenser section rear portion, the close air outlet slit place of described blower setting in dehumidifying casing, the air port of described pressure fan is communicated with air outlet slit, air in drying baker is in air intlet enters dehumidifying casing, successively through heat pipe evaporator section, evaporimeter, heat pipe condenser section and condenser are circulated to air outlet slit place, pressure fan is sent into the air that is circulated to air outlet slit place in drying baker.
Concrete, in described dehumidifying casing, separate and be divided into upper box and lower box by dividing plate, described air intlet and air outlet slit are opened in the same sidepiece of dehumidifying casing, described air intlet is communicated with lower box, described air outlet slit is positioned at air intlet top and is communicated with upper box, also offers the air vent that is communicated with upper box and lower box on described dividing plate.
Further, described air vent is positioned on dividing plate away from air intlet and air outlet slit place, described heat pipe is erected in lower box and stretches in upper box, the part that described heat pipe is positioned at lower box forms heat pipe evaporator section, the part that described heat pipe is positioned at upper box forms heat pipe condenser section, described evaporimeter and condenser are all arranged in upper box, and described evaporimeter is between heat pipe condenser section and air vent, and described condenser is between heat pipe condenser section and pressure fan.
Preferably, be provided with lower water deflector in described lower box, in described upper box, be provided with water deflector, described lower water deflector is erected between heat pipe evaporator section and air vent, and described upper water deflector is erected between heat pipe condenser section and evaporimeter.
Further, described dehydrating unit also comprises the lower water accumulating disc being arranged in lower box and is arranged on the upper water accumulating disc in upper box, described lower water accumulating disc is positioned at the below of heat pipe evaporator section and lower water deflector, upper water accumulating disc is positioned at the below of described evaporimeter and upper water deflector, described upper water accumulating disc and lower water accumulating disc pass through pipeline connection, the bottom of described lower box offers discharge outlet, and described lower water accumulating disc is communicated with discharge outlet by pipeline.
Concrete, described refrigeration system also comprises expansion valve, compressor and gas-liquid separator, described condenser, expansion valve, evaporimeter is connected by pipeline successively with gas-liquid separator, the high-voltage output end of described compressor is connected with condenser by pipeline, the low pressure input of described compressor is connected with the output of gas-liquid separator by pipeline, described compressor operating output gaseous refrigerant enters condenser and carries out becoming liquid refrigerant after heat exchange through the air of condenser, liquid refrigerant changes the cold-producing medium of gas-liquid two-phase into through expansion valve, the cold-producing medium of gas-liquid two-phase is through evaporimeter and flash to gaseous refrigerant after the air heat-exchange of evaporimeter, gaseous refrigerant returns to compressor after by gas-liquid separator separates.
Scope of the present invention, is not limited to the technical scheme that the particular combinations of above-mentioned technical characterictic forms, and also should contain by above-mentioned technical characterictic or its equivalent feature and be combined and other technical scheme of forming simultaneously. The technical characterictic that such as, in above-mentioned feature and the application disclosed (but being not limited to) has a similar functions is replaced mutually and technical scheme of forming etc.
Because technique scheme is used; the present invention compared with prior art has following advantages: adopt dehydrating unit to carry out non-stop-machine ventilation dehumidifying to air in drying baker; make drying baker only need be heated to 50 DEG C of oven dry that can realize parts; good drying effect; improve bake out temperature without further heating, save electric energy. Meanwhile, dehydrating unit be under the non-stop-machine state of drying baker to drying baker in air dehumidify, greatly improved the operating efficiency of dryer.
Brief description of the drawings
Fig. 1 is the structure principle chart of a kind of dryer of the present invention;
Fig. 2 is the structure principle chart of refrigeration system in a kind of dryer of the present invention;
Wherein: 1, dehumidifying casing; 2, heat pipe; 3, pressure fan; 4, evaporimeter; 5, condenser; 6, lower water deflector; 7, upper water deflector; 8, lower water accumulating disc; 9, upper water accumulating disc; 11, air intlet; 12, air outlet slit; 13, dividing plate; 14, upper box; 15, lower box; 16, air vent; 17, discharge outlet; 21, heat pipe evaporator section; 22, heat pipe condenser section; 101, expansion valve; 102, compressor; 103, gas-liquid separator; 104, filter.
Detailed description of the invention
As depicted in figs. 1 and 2, the dehydrating unit 100 that a kind of dryer comprises drying baker (not shown) and docks with drying baker. Described dehydrating unit 100 can be removed contained moisture in the interior air of drying baker. Described dehydrating unit 100 comprises dehumidifying casing 1 and is arranged on heat pipe 2, refrigeration system and the pressure fan 3 in dehumidifying casing 1. In described dehumidifying casing 1, separate and be divided into upper box 14 and lower box 15 by dividing plate 13. On described dehumidifying casing 1, offer the air intlet 11 and the air outlet slit 12 that are communicated with drying baker respectively, described air intlet 11 and air outlet slit 12 are positioned at the same sidepiece of dehumidifying casing 1. Described air intlet 11 is communicated with lower box 15, described air outlet slit 12 is positioned at air intlet 11 tops and is communicated with upper box 14, on described dividing plate 13, also offer the air vent 16 that is communicated with upper box 14 and lower box 15, described air vent 16 be positioned at dividing plate 13 away from air intlet 11 and air outlet slit 12 places. In described dehumidifying casing 1, form circulation of air air channel from air intlet 11 through air vent 16 to air outlet slit 12.
Described heat pipe 2 is erected in lower box 15 and stretches in upper box 14. The part that described heat pipe 2 is positioned at lower box 15 forms heat pipe evaporator section 21, and the part that described heat pipe 2 is positioned at upper box 14 forms heat pipe condenser section 22. The operation principle of described heat pipe 2 is as described below: in heat pipe 2, be injected with cold-producing medium. In heat pipe evaporator section 21, be full of liquid refrigerant, in the time that hot and humid air passes through heat pipe evaporator section 21, the cold-producing medium that liquid refrigerant heat absorption evaporation wherein becomes gaseous state carries out precooling to hot and humid air simultaneously. In heat pipe 2, the cold-producing medium of gaseous state can rise to the first half of heat pipe, i.e. heat pipe condenser section 22. When the air of low temperature and low humidity is during through the condensation segment 22 of superheater tube, in heat pipe 2, the cold-producing medium heat release of gaseous state is condensed into liquid cold-producing medium, the air of low temperature and low humidity is carried out to preheating simultaneously. Be condensed into the latter half that liquid cold-producing medium can drop to heat pipe 2, heat pipe evaporator section 21, so, completes a heat exchange cyclic process.
Described pressure fan 3 is arranged on close air outlet slit 12 places in dehumidifying casing 1, and the air port of described pressure fan 3 is communicated with air outlet slit 12. Described refrigeration system comprises the evaporimeter 4 that is arranged on heat pipe evaporator section 21 rear portions and the condenser 5 that is arranged on heat pipe condenser section 22 rear portions. Described evaporimeter 4 and condenser 5 are all positioned at upper box 14, and described evaporimeter 4 is between heat pipe condenser section 22 and air vent 16, and described condenser 5 is between heat pipe condenser section 22 and pressure fan 3. Air in drying baker, in air intlet 11 enters dehumidifying casing 1, is circulated to air outlet slit 12 places through heat pipe evaporator section 21, evaporimeter 4, heat pipe condenser section 22 and condenser 5 successively, and pressure fan 3 is sent into the air that is circulated to air outlet slit 12 places in drying baker.
In described lower box 15, be provided with lower water deflector 6, in described upper box 14, be provided with water deflector 7, described lower water deflector 6 is erected between heat pipe evaporator section 21 and air vent 16, and described upper water deflector 7 is erected between heat pipe condenser section 22 and evaporimeter 5 and is fitted in heat pipe condenser section 22 places.
Described dehydrating unit 1 also comprises the lower water accumulating disc 8 being arranged in lower box 15 and is arranged on the upper water accumulating disc 9 in upper box 14. Described lower water accumulating disc 8 is positioned at the below of heat pipe evaporator section 21 and lower water deflector 6, and upper water accumulating disc 9 is positioned at the below of described evaporimeter 4 and upper water deflector 7. Described upper water accumulating disc 9 and lower water accumulating disc 8 are by pipeline connection, and the bottom of described lower box 15 offers discharge outlet 17, and described lower water accumulating disc 8 is communicated with discharge outlet 17 by pipeline. Described upper water deflector 7 is assembled the water of condensation in air to flow in upper water accumulating disc 9, and described lower water deflector 6 is assembled the water of condensation in air to flow in lower water accumulating disc 8. The condensed water of upper water accumulating disc 9 interior Shengs flows in lower water accumulating disc 8 by the road. Condensed water in lower water accumulating disc 8 flows out dehumidifying casing 1 from discharge outlet 17 by the road.
The course of work of dryer of the present invention is as follows:
In drying baker, dry to the parts that are placed in drying baker air heat to 50 DEG C left and right by electrically heated mode. Parts in drying baker are because of heating, and its surperficial moisture evaporation is mixed to form hot and humid air with hot-air, and hot and humid air enters in lower box 15 by air intlet 11. The hot and humid air of process is carried out precooling by heat pipe evaporator section 21, and hot and humid air becomes the air of middle temperature high humidity. The air of middle temperature high humidity is tackled through lower water deflector 6, and wherein part steam condenses into liquid in the lower water accumulating disc 8 of lower water deflector 6 inflow belows. The air of middle temperature high humidity is circulated in upper box 15 from air vent 16, pass through the again cooling of evaporimeter 4, steam in the air of middle temperature high humidity is cooled to dew point and condenses into condensed water and separate out, the condensed water of separating out flows in the upper water accumulating disc 9 of below through the interception of upper water deflector 7, and the air of middle temperature high humidity becomes the air of low temperature and low humidity. The air of low temperature and low humidity becomes the air of middle temperature low humidity through the preheating of heat pipe condenser section 22. The air of middle temperature low humidity passes through condenser 5 again, raises and forms the air of high temperature low humidity with the cold-producing medium heat-exchange temperature in condenser 5. The air of final high temperature low humidity is sent back in drying baker through air outlet slit 12 by pressure fan 3. Complete like this circulation of air dewetting, the airborne steam in drying baker is removed, and makes the better effects if of drying baker inner heating drying parts, dries the temperature inside the box without being heated to 90 DEG C of above hot operations, saves electric energy. Drying baker can be worked parts are dried always, and without shutting down dehumidifying, operating efficiency improves greatly.
As shown in Figure 2, the refrigeration system in the present invention also comprises expansion valve 101, compressor 102, gas-liquid separator 103 and filter 104. Described compressor 102 and gas-liquid separator 103 are all arranged in lower box 15. Described condenser 5, filter 104, expansion valve 101, evaporimeter 5 and gas-liquid separator 103 are connected successively by pipeline. The high-voltage output end of described compressor 102 is connected with condenser 5 by pipeline, and the low pressure input of described compressor 102 is connected with the output of gas-liquid separator 103 by pipeline. The refrigerant gas of described compressor 102 work output HTHPs enters condenser 5 and carries out heat exchange with the air of the middle temperature low humidity through condenser 5. The liquid refrigerant of the condensation of refrigerant Cheng Zhongwen high pressure of HTHP, meanwhile, the air of middle temperature low humidity is heated to form the air of high temperature low humidity. The liquid refrigerant of middle temperature high pressure filters the cold-producing medium that changes again gas-liquid two-phase through expansion valve 101 into through filter 104. The cold-producing medium of gas-liquid two-phase is the air heat-exchange with the middle temperature high humidity through evaporimeter 4 through evaporimeter 4. The cold-producing medium evaporation of gas-liquid two-phase is gaseous refrigerant, and in the while, the air of warm high humidity is lowered the temperature, and water vapor condensation becomes aqueous water, the air of the dehumidified one-tenth low temperature and low humidity of air of middle temperature high humidity. Gaseous refrigerant returns to compressor 102 after separating by gas-liquid separator 103, completes a cyclic process of dehumidifying.
As mentioned above, we are illustrated according to aim of the present invention completely, but the present invention is not limited to above-described embodiment and implementation method. The practitioner of correlative technology field can carry out different variations and enforcement in the scope of technological thought license of the present invention.
Claims (6)
1. a dryer, it is characterized in that: the dehydrating unit (100) that comprises drying baker and dock with drying baker, described dehydrating unit (100) can be removed contained moisture in the interior air of drying baker, described dehydrating unit (100) comprises dehumidifying casing (1), with the heat pipe (2) being arranged in dehumidifying casing (1), refrigeration system and pressure fan (3), on described dehumidifying casing (1), offer the air intlet (11) and the air outlet slit (12) that are communicated with drying baker respectively, in described dehumidifying casing (1), form circulation of air air channel from air intlet (11) to air outlet slit (12), described heat pipe (2) is erected in dehumidifying casing (1), heat pipe evaporator section (21) is formed at the bottom of described heat pipe (2), heat pipe condenser section (22) is formed at the top of described heat pipe (2), described refrigeration system comprises the condenser (5) that is arranged on the evaporimeter (4) at heat pipe evaporator section (21) rear portion and is arranged on heat pipe condenser section (22) rear portion, the close air outlet slit (12) that described pressure fan (3) is arranged in dehumidifying casing (1) is located, the air port of described pressure fan (3) is communicated with air outlet slit (12), air in drying baker is in air intlet (11) enters dehumidifying casing (1), successively through heat pipe evaporator section (21), evaporimeter (4), heat pipe condenser section (22) and condenser (5) are circulated to air outlet slit (12) and locate, pressure fan (3) is sent in drying baker being circulated to the air that air outlet slit (12) locates.
2. a kind of dryer according to claim 1, it is characterized in that: in described dehumidifying casing (1), separate and be divided into upper box (14) and lower box (15) by dividing plate (13), described air intlet (11) and air outlet slit (12) are opened in the same sidepiece of dehumidifying casing (1), described air intlet (11) is communicated with lower box (15), described air outlet slit (12) is positioned at air intlet (11) top and is communicated with upper box (14), also offers the air vent (16) that is communicated with upper box (14) and lower box (15) on described dividing plate (13).
3. a kind of dryer according to claim 2, it is characterized in that: described air vent (16) is positioned at dividing plate (13) and above locates away from air intlet (11) and air outlet slit (12), described heat pipe (2) is erected in lower box (15) and stretches in upper box (14), the part that described heat pipe (2) is positioned at lower box (15) forms heat pipe evaporator section (21), the part that described heat pipe (2) is positioned at upper box (14) forms heat pipe condenser section (22), described evaporimeter (4) and condenser (5) are all arranged in upper box (14), described evaporimeter (4) is positioned between heat pipe condenser section (22) and air vent (16), described condenser (5) is positioned between heat pipe condenser section (22) and pressure fan (3).
4. a kind of dryer according to claim 3, it is characterized in that: in described lower box (15), be provided with lower water deflector (6), in described upper box (14), be provided with water deflector (7), described lower water deflector (6) is erected between heat pipe evaporator section (21) and air vent (16), and described upper water deflector (7) is erected between heat pipe condenser section (22) and evaporimeter (5).
5. a kind of dryer according to claim 4, it is characterized in that: described dehydrating unit (1) also comprises and is arranged on the lower water accumulating disc (8) in lower box (15) and is arranged on the interior upper water accumulating disc (9) of upper box (14), described lower water accumulating disc (8) is positioned at the below of heat pipe evaporator section (21) and lower water deflector (6), upper water accumulating disc (9) is positioned at the below of described evaporimeter (4) and upper water deflector (7), described upper water accumulating disc (9) and lower water accumulating disc (8) pass through pipeline connection, the bottom of described lower box (15) offers discharge outlet (17), described lower water accumulating disc (8) is communicated with discharge outlet (17) by pipeline.
6. a kind of dryer according to claim 1, it is characterized in that: described refrigeration system also comprises expansion valve (101), compressor (102) and gas-liquid separator (103), described condenser (5), expansion valve (101), evaporimeter (5) is connected by pipeline successively with gas-liquid separator (103), the high-voltage output end of described compressor (102) is connected with condenser (5) by pipeline, the low pressure input of described compressor (102) is connected with the output of gas-liquid separator (103) by pipeline, described compressor (102) work output gaseous refrigerant enters condenser (5) and carries out becoming liquid refrigerant after heat exchange through the air of condenser (5), liquid refrigerant changes the cold-producing medium of gas-liquid two-phase into through expansion valve (101), the cold-producing medium of gas-liquid two-phase forms gaseous refrigerant through evaporimeter (4) and evaporation after the air heat-exchange of evaporimeter (4), gaseous refrigerant returns to compressor (102) after separating by gas-liquid separator (103).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610183397.1A CN105605911A (en) | 2016-03-29 | 2016-03-29 | Drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610183397.1A CN105605911A (en) | 2016-03-29 | 2016-03-29 | Drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105605911A true CN105605911A (en) | 2016-05-25 |
Family
ID=55986051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610183397.1A Pending CN105605911A (en) | 2016-03-29 | 2016-03-29 | Drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105605911A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105841259A (en) * | 2016-05-26 | 2016-08-10 | 天津大学 | Energy-saving dehumidifier additionally provided with pulsating heat pipe |
| CN107525355A (en) * | 2016-06-22 | 2017-12-29 | 杭州三花家电热管理系统有限公司 | Heat-pump-type drying unit |
| CN109708330A (en) * | 2018-11-30 | 2019-05-03 | 安徽欧瑞达电器科技有限公司 | A kind of cell liquid recycling unit |
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| CN2336303Y (en) * | 1998-05-23 | 1999-09-01 | 唐晓宇 | Energy-saving heat-pipe dehumidifying case |
| US6321460B1 (en) * | 1999-12-23 | 2001-11-27 | Keum Su Jin | Drying apparatus |
| CN201569247U (en) * | 2009-10-10 | 2010-09-01 | 彭福明 | Thermal pump dehumidification drying machine |
| CN103123215A (en) * | 2013-03-11 | 2013-05-29 | 孙应真 | Intelligent hot-air drying control device |
| CN103256801A (en) * | 2012-02-18 | 2013-08-21 | 中山火炬职业技术学院 | Drying method combing heat pump drying, heat tube drying and microwave drying |
| CN203758206U (en) * | 2014-03-10 | 2014-08-06 | 广东机电职业技术学院 | Heat pump drying machine with heat pipe heat recovery device |
| CN205403433U (en) * | 2016-03-29 | 2016-07-27 | 苏州苏净安发空调有限公司 | Drying machine |
-
2016
- 2016-03-29 CN CN201610183397.1A patent/CN105605911A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2336303Y (en) * | 1998-05-23 | 1999-09-01 | 唐晓宇 | Energy-saving heat-pipe dehumidifying case |
| US6321460B1 (en) * | 1999-12-23 | 2001-11-27 | Keum Su Jin | Drying apparatus |
| CN201569247U (en) * | 2009-10-10 | 2010-09-01 | 彭福明 | Thermal pump dehumidification drying machine |
| CN103256801A (en) * | 2012-02-18 | 2013-08-21 | 中山火炬职业技术学院 | Drying method combing heat pump drying, heat tube drying and microwave drying |
| CN103123215A (en) * | 2013-03-11 | 2013-05-29 | 孙应真 | Intelligent hot-air drying control device |
| CN203758206U (en) * | 2014-03-10 | 2014-08-06 | 广东机电职业技术学院 | Heat pump drying machine with heat pipe heat recovery device |
| CN205403433U (en) * | 2016-03-29 | 2016-07-27 | 苏州苏净安发空调有限公司 | Drying machine |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105841259A (en) * | 2016-05-26 | 2016-08-10 | 天津大学 | Energy-saving dehumidifier additionally provided with pulsating heat pipe |
| CN107525355A (en) * | 2016-06-22 | 2017-12-29 | 杭州三花家电热管理系统有限公司 | Heat-pump-type drying unit |
| CN109708330A (en) * | 2018-11-30 | 2019-05-03 | 安徽欧瑞达电器科技有限公司 | A kind of cell liquid recycling unit |
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Application publication date: 20160525 |