CN212299865U - Air energy heat pump dryer - Google Patents

Air energy heat pump dryer Download PDF

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Publication number
CN212299865U
CN212299865U CN202020258412.6U CN202020258412U CN212299865U CN 212299865 U CN212299865 U CN 212299865U CN 202020258412 U CN202020258412 U CN 202020258412U CN 212299865 U CN212299865 U CN 212299865U
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China
Prior art keywords
air
heat pump
valve
heat exchange
evaporator
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CN202020258412.6U
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Chinese (zh)
Inventor
朱超
罗婷
刘富贵
武懿
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Hunan Shuifa Xingye Technology Co ltd
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Hunan Singyes Solar Technology Co ltd
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Abstract

The utility model discloses an air energy heat pump drying-machine, including circulating fan group, total heat exchange core, evaporation fan, air energy heat pump system and wind net, the drying-machine is separated into roughly three relatively independent cavity about left side, right side by inside panel beating, the wind net is located the right side of right side cavity, total heat exchange core transversely sets up at drying-machine left side middle part, and four independent cavities about the left and right sides about the inside is cut apart into through inside panel beating based on total heat exchange core of left side organism, the drying-machine changes the inside hot air circulation route of drying-machine through the switch between the electronic blast gate of control to realize heating, three kinds of operating modes of hydrofuge and dehumidification under the condition that only uses single evaporimeter of single set air source heat pump system. Meanwhile, the full heat exchange core and the special dehumidification method are used, so that the unit can recover a large amount of heat energy under the dehumidification working condition, and the energy efficiency of the unit is obviously improved.

Description

Air energy heat pump dryer
Technical Field
The utility model relates to a crops stoving technical field specifically is an air energy heat pump drying-machine.
Background
In the field of agricultural product drying at present, the application of the air source heat pump dryer is more and more extensive, the trend of comprehensively replacing original coal and gas for drying is achieved, governments are vigorously popularized, and the effects of energy conservation and emission reduction are remarkable.
Agricultural product kind is various, and stoving processing technology is different, for the stoving demand that satisfies different products, and the air source drying-machine in present stage mainly divide into the hydrofuge and dehumidifies two main categories, is difficult to compatible between the different grade type stoving mode, and the unit that a small number can satisfy the dual mode simultaneously often adopts and sets up two sets of evaporimeters in order to satisfy different operating mode demands, and the structure is complicated. Accordingly, one skilled in the art provides an air energy heat pump dryer to solve the problems set forth in the background art.
Disclosure of Invention
An object of the utility model is to provide an air energy heat pump drying-machine to solve the problem that proposes among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
an air energy heat pump dehumidification dryer comprises a circulating fan set, a total heat exchange core body, an evaporation fan, an air energy heat pump system and an air net, wherein the dryer is divided into three relatively independent chambers which are roughly divided into a left chamber, a middle chamber and a right chamber by an internal metal plate, the air net is positioned on the right side of the right chamber, the total heat exchange core body is transversely arranged in the middle of the left side of the dryer, the inside of a left machine body is divided into an upper independent chamber, a lower independent chamber, a left independent chamber and a right independent chamber by the internal metal plate based on the total heat exchange core body, the upper independent chamber, the lower independent chamber, the left independent chamber, the upper independent chamber and the right independent chamber respectively correspond to four air inlet and outlet surfaces of the total heat exchange core body, the total heat exchange core body is communicated with two diagonal chambers, the circulating fan set is arranged at the lower part of the left side of the machine body, the flow direction of, the right side of the cavity on the upper right side is provided with a third electric air valve, the right side of the cavity on the lower right side is provided with a fourth electric air valve, the evaporation fan unit is arranged in the middle of the machine body, an air outlet is upward, and the flow direction is from inside to outside; the evaporator is arranged in the middle of the dryer and between the evaporation fan set and the air valve; the compressor, the throttling device and other accessories are arranged on the rightmost side of the unit, the dryer changes a hot air circulation path inside the dryer by controlling a switch between electric air valves, so that two working conditions of heating, drying and dehumidifying are realized under the condition that only a single air source heat pump system and a single evaporator are used, and meanwhile, a large amount of heat energy is recovered by the unit under the dehumidifying working condition due to the use of a total heat exchange core body and a special dehumidifying method, and the energy efficiency of the unit is remarkably improved.
As a further proposal of the utility model, the evaporator adopts a multi-path design, and every path of heat exchanger passage is relatively independent
As the utility model discloses further scheme, pipeline between evaporimeter and the expansion valve divide into the multichannel, and every way all is provided with normally open solenoid valve, and thereby reduce evaporimeter pipeline through the solenoid valve that closes a road number under the dehumidification operating mode, reduce evaporimeter heat transfer area and reduce evaporating temperature and guarantee unit steady operation.
As the utility model discloses further scheme, the evaporation fan is the frequency conversion fan, adjusts the amount of wind of flowing through the evaporimeter through control and with control system's evaporating temperature, guarantees the steady operation under the various operating modes.
As the utility model discloses further scheme, full heat exchange core and evaporimeter bottom are provided with the water collector, and the water collector passes through the water discharging nozzle and links to each other with plastic hose, and the hose leads to the unit outside for the comdenstion water that produces when full heat exchange core and evaporimeter heat exchange can discharge the unit smoothly, is unlikely to the siltation and leads to the unit heat preservation ability to descend, the panel beating corrosion in the unit.
As a further scheme of the utility model, electronic blast gate one and electronic blast gate three remove "close entirely" and "open entirely" two shelves and still be equipped with "half-open" one shelves, during the unit dehumidification operating mode, electronic blast gate one, three "half-open" need not set up special exhaust fan in addition and can reach the dehumidification effect.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the utility model discloses a switch action of control electronic blast gate can change the air and with the route at the inside stream of unit, realizes the heating, the hydrofuge, the seamless switching between the three big operating modes of dehumidification.
2. The utility model discloses an air source heat pump system only needs to set up one set of evaporimeter alone, from external heat absorption's heat exchanger when both regarding as heating and dehumidification operating mode, dehumidifier when also regarding as the dehumidification operating mode.
3. The utility model discloses a multitube way between evaporimeter and expansion valve, the setting of solenoid valve to and evaporation fan frequency conversion control, realize the controllability of evaporation area and the evaporation amount of wind, guarantee the steady operation of unit heat pump system when each operating mode switches.
Drawings
Fig. 1 is a working schematic diagram of a heating condition of an air-source heat pump dryer.
Fig. 2 is a schematic diagram of the operation of an air energy heat pump dryer under dehumidification conditions.
Fig. 3 is a schematic diagram of the operation of the air energy heat pump dryer in the dehumidification mode.
Fig. 4 is a schematic structural diagram of an air-source heat pump dryer.
In the figure: 1. a circulating fan unit; 2. a condenser; 3. an evaporator; 4. an evaporation fan; 5. a total heat exchange core; 6. a first electric air valve; 7. a second electric air valve; 8. a third electric air valve; 9. an air outlet valve; 10. a fourth electric air valve; 11. an air inlet valve; 12. a compressor; 13. a wind net; 14. an electromagnetic valve; 15. an expansion valve; 16. a first water receiving plate; 17. and a second water receiving tray.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, in the embodiment of the present invention, an air energy heat pump dryer is provided, which includes a circulating fan assembly 1, a total heat exchange core 5, an evaporation fan 4, an air energy heat pump system and an air network 13, the dryer is divided into three relatively independent chambers, i.e. a left chamber, a middle chamber and a right chamber, by an internal metal plate, the air network 13 is located on the right side of the right chamber, the total heat exchange core 5 is transversely disposed in the middle of the left chamber of the dryer, four edges of the total heat exchange core are respectively connected with the metal plate of the dryer to divide the interior of the dryer into four independent chambers, the total heat exchange core 5 is connected with two diagonal chambers, the circulating fan assembly 1 is disposed on the lower left portion of the outer side of the dryer, an air outlet is outward, the right side of the circulating fan assembly 1 is connected with a condenser 2, the condenser 2 is located in the chamber on the, the upper side of the cavity on the upper right side is provided with an electric air valve II 7, the right side of the cavity on the upper right side is provided with an electric air valve III 8, and the right side of the cavity on the lower right side is provided with an electric air valve IV 10;
the first electric air valve 6 and the third electric air valve 8 are provided with an air outlet valve 9 above a middle cavity of a half-open gear body besides opening and closing, the air outlet valve 9 is downwards sequentially provided with an evaporator 3, an evaporation fan 4 and an air inlet valve 11, and the air inlet valve 11 is arranged on the lower right side of the middle cavity of the body; the evaporation fan 4 is transversely arranged in the middle of the cavity in the middle of the machine body, and the air outlet direction is upward; the air energy heat pump system comprises a condenser 2, a compressor 12, an evaporator 3 and an expansion valve 15, wherein a second water pan 17 is arranged at the lower part of the evaporator 3, a first water pan 16 is arranged at the lower part of the total heat exchange core body 5, and the condenser 2 is arranged in a cavity at the lower left side of the total heat exchange core body 5; the evaporator 3 is obliquely arranged between the evaporation fan 4 and the air outlet valve of the electric air valve 9, the evaporation fan 4 adopts a variable frequency fan or a gear adjustable fan, the evaporator 3 adopts a multi-path design, and the path of each heat exchanger is relatively independent; the compressor 12 is arranged at the lower part of the right chamber of the machine body; the expansion valve 15 is arranged between the condenser 2 and the evaporator 3 along the heat pump system pipeline, the expansion valve 15 and the evaporator 3 are connected by a plurality of pipelines corresponding to each passage of the evaporator 3, and each pipeline is provided with an electromagnetic valve 14 for controlling the on-off of the pipeline.
The utility model discloses a theory of operation is:
as shown in fig. 1, when an air energy heat pump dryer is in a heating working condition, a second electric air valve 7, an air inlet valve 11 and an air outlet valve 9 of a unit are in a fully open state, and the rest air valves are in a fully closed state. The outside air passes through the air net 13, is blown through the evaporator 3 by the evaporation fan 4 via the air inlet valve 11 to do work, then returns to the outside through the air outlet valve 9, and the condensed water generated in the heat absorption process of the evaporator 3 is led out of the machine body by the second water receiving disc 17; and return air of the drying room enters the unit through the electric air valve II 7, passes through the total heat exchange core body 5, is heated through the condenser 2 and is conveyed into the drying room through the circulating fan unit 1. Thereby realizing the drying and heating process.
As shown in fig. 2, when an air energy heat pump dryer is in a dehumidification working condition, a first electric air valve 6, a third electric air valve 8 and a fourth electric air valve 10 of a unit are opened to be in a fully-opened state, and the other air valves are fully closed. The return air of the drying room enters the unit through the first electric air valve 6, is conveyed to the evaporator 3 through the fourth electric air valve 10 by the evaporation fan 4 after passing through the total heat exchange core 5, is subjected to heat absorption, is reduced in temperature and moisture content, is heated through the condenser 2 after passing through the other group of channels of the total heat exchange core 5 again through the third electric air valve 8, is conveyed into the drying room through the circulating air unit 1, and the condensed water generated by dehumidification at the position of the evaporator 3 is discharged out of the unit body through the second water receiving disc 17. Thereby realizing the drying and dehumidifying process.
In the process, the two groups of channels of the total heat exchange core body 5 have temperature difference due to heat absorption of the evaporator 3, so that a heat exchange process exists, and the generated condensed water is discharged out of the machine body through the first water receiving disc 16. When the exhaust temperature of the air source heat pump system is higher, the electromagnetic valves 14 between one group or multiple groups of evaporators 3 and the expansion valve 15 are correspondingly closed, the output power of the evaporation fan 4 is controlled, the evaporation area and the evaporation air volume of the system are adjusted, and the stable dehumidification of the unit is ensured.
As shown in fig. 3, when an air-source heat pump dryer is in a dehumidification condition, the operation state of the unit is similar to that in the heating condition corresponding to fig. 1. The difference is that at the moment, the first electric air valve 6 and the third electric air valve 8 are in a half-open state, and the rest air valves are all opened to be fully-open. Due to the influence of the evaporation fan 4, the return air of the drying room mostly enters the machine body through the electric air valve II 7, and the small part enters the machine body through the electric air valve I6, and the wet air of the part flows out of the electric air valve IV 10 after passing through the total heat exchange core body 5 and is mixed with the external air entering from the air inlet valve 11, and then is conveyed through the evaporation fan 4, and the evaporator 3 absorbs heat and is discharged out of the machine body from the air outlet valve 9; meanwhile, due to the influence of the circulating fan unit 1, part of dry and cold air which absorbs heat through the evaporator 3 enters the machine body through the electric air valve III 8, is mixed with hot air entering from the electric air valve II 7, passes through the other group of channels of the total heat exchange core body 5, is heated at the condenser 2, and is conveyed into the drying room through the circulating fan unit 1. Thereby realizing the drying and dehumidifying process.
In the process, the path of the high-temperature and high-humidity air exhausted by the unit passes through the evaporator 3, the evaporation temperature is increased to a certain extent, and a part of heat energy is recovered; the fresh air entering the unit is low-humidity air subjected to heat absorption and dehumidification through the evaporator 3, and the initial moisture content is far smaller than that of the outside air; at the total heat exchange core body 5, low-temperature fresh air entering the unit and damp and hot air to be discharged out of the unit respectively flow through different channels, so that heat exchange is carried out, a part of heat energy is recovered, and simultaneously generated condensation is led out of the machine body from the water receiving disc I16. The processes improve the drying efficiency to a certain extent, and are beneficial to the drying process
The inside hot-blast circulation route of drying-machine is changed through the switch between the electronic blast gate of control to the drying-machine to only realize heating, three kinds of operating modes of dehumidification and dehumidification under the condition of using single set of air source heat pump system single evaporimeter. Meanwhile, the full heat exchange core and the special dehumidification method are used, so that the unit can recover a large amount of heat energy under the dehumidification working condition, and the energy efficiency of the unit is obviously improved.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.

Claims (6)

1. The utility model provides an air can heat pump drying-machine, includes circulating fan group (1), total heat exchange core (5), evaporating fan (4), air can heat pump system and wind net (13), characterized by: the dryer is divided into three relatively independent chambers which are approximately from left to right by an internal metal plate, the air net (13) is positioned on the right side of the chamber on the right side, the total heat exchange core body (5) is transversely arranged in the middle of the chamber on the left side of the dryer body, four edges are respectively connected with the sheet metal of the dryer body to divide the inside of the dryer body on the left side into four independent chambers, the total heat exchange core body (5) is communicated with two diagonal chambers, the circulating fan group (1) is arranged on the left lower part of the outer side of the dryer body, an air outlet faces outwards, the right side of the circulating fan group (1) is communicated with the condenser (2), the condenser (2) is positioned in the chamber on the lower left side, the chamber on the upper left side is provided with the electric air valve I (6), the electric air valve I (6) is communicated with the chamber, the upper side of the chamber on the upper right side is provided with, an air outlet valve (9) is arranged above the middle cavity of the machine body, an evaporator (3), an evaporation fan (4) and an air inlet valve (11) are sequentially arranged on the air outlet valve (9) downwards, and the air inlet valve (11) is arranged on the lower right side of the middle cavity of the machine body; the evaporation fan (4) is transversely arranged in the middle of a cavity in the middle of the machine body, the air outlet is upward, the air energy heat pump system comprises a condenser (2), a compressor (12), an evaporator (3) and an expansion valve (15), the condenser (2) is arranged in the cavity at the lower left side of the total heat exchange core body (5), and the evaporator (3) is obliquely arranged between the evaporation fan (4) and the air outlet valve (9); the compressor (12) is arranged at the lower part of the right chamber of the machine body; the expansion valve (15) is arranged between the condenser (2) and the evaporator (3) along the heat pump system pipeline.
2. An air-source heat pump dryer according to claim 1, characterized in that the evaporator (3) is of a multi-pass design, each heat exchanger pass being relatively independent.
3. An air-source heat pump dryer according to claim 1, characterized in that the expansion valve (15) and the evaporator (3) are connected in a plurality of pipelines corresponding to each passage of the evaporator (3), and each pipeline is provided with a solenoid valve (14) for controlling the on-off of the pipeline.
4. An air-source heat pump dryer according to claim 1, characterized in that the evaporation fan (4) is a variable frequency fan or a gear-adjustable fan.
5. An air-source heat pump dryer according to claim 1, characterized in that a second water-receiving tray (17) is arranged at the lower part of the evaporator (3), and a first water-receiving tray (16) is arranged at the lower part of the total heat exchange core (5).
6. The air-source heat pump dryer as claimed in claim 1, wherein the first electric air valve (6) and the third electric air valve (8) are provided with a half-open gear in addition to being opened and closed.
CN202020258412.6U 2020-03-05 2020-03-05 Air energy heat pump dryer Active CN212299865U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020258412.6U CN212299865U (en) 2020-03-05 2020-03-05 Air energy heat pump dryer

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Application Number Priority Date Filing Date Title
CN202020258412.6U CN212299865U (en) 2020-03-05 2020-03-05 Air energy heat pump dryer

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CN212299865U true CN212299865U (en) 2021-01-05

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114674138A (en) * 2022-05-27 2022-06-28 杭州宏华数码科技股份有限公司 Method, computing device, and medium for controlling drying of objects to be dried

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114674138A (en) * 2022-05-27 2022-06-28 杭州宏华数码科技股份有限公司 Method, computing device, and medium for controlling drying of objects to be dried

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Address after: 411100 No.1 Xingye Avenue, Jiuhua Economic Zone, Xiangtan City, Hunan Province

Patentee after: Hunan Shuifa Xingye Technology Co.,Ltd.

Address before: 411100 No.1 Xingye Avenue, Jiuhua Economic Zone, Xiangtan City, Hunan Province

Patentee before: HUNAN SINGYES SOLAR TECHNOLOGY Co.,Ltd.

CP01 Change in the name or title of a patent holder