CN103900289A - System and method for preventing air source heat pump water heater from frosting by using solid dehumidification - Google Patents
System and method for preventing air source heat pump water heater from frosting by using solid dehumidification Download PDFInfo
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Abstract
The invention provides a system and method for preventing an air source heat pump water heater from frosting by using solid dehumidification. In the method, a heat exchanger with a solid drying agent coating is used for preprocessing water in moist air, and therefore the water in the moist air is prevented from frosting on the surface of an evaporator. According to the system and method, the air of an inlet of the evaporator is dehumidified by means of the solid drying agent coating, so that the frosting problem of the heat pump water heater is resolved, and heating performance of the heat pump water heater is enhanced. When the water absorbed by solid adsorbing agents reaches a limitation, water in the solid adsorbing agents is desorbed by means of heat released by condensation of heat pump work media, at this time, circulation air with desorbed high-temperature moisture has heat exchange and congeals on the surface of the evaporator, the evaporator recycles the heat released in a condenser, and regeneration efficiency of a heat pump is improved.
Description
Technical field
The present invention utilizes solution to carry out dehumidification treatments to the air in Teat pump boiler loop, improve the outdoor evaporimeter heat exchange property of Teat pump boiler, improve the heating performance of heat pump water heater system, belong to and improve air source hot pump water heater performance field, relate to household electrical appliances and manufacture field, especially, combine a kind of method of pre-antifrost.
Background technology
At present, in the water heater that China resident uses, electric heater, gas heater and solar water heater occupy great ratio.And in air source hot pump water heater can need the transfer of heat of low-temperature heat source by consumption part electric energy domestic hot-water to us, because its energy-efficient advantage becomes the 4th class New-type water heater form.But it is subject to the impact of region temperature, the area of low, the high humidity of outside air temperature in the winter time, the situation in evaporator surface generation frosting very easily when it's the end is past the evaporating temperature of heat pump, thereby affect the heat transfer effect of evaporimeter, cause system heating capacity to reduce, the heating performance of heat pump reduces, and in serious situation, even can not start.For this problem, the method for multiple solution defrosting has been proposed both at home and abroad, comprise nature defrosting, hot gas defrosting, water defrosting and electric heated defrosting etc.What the air source hot pump water heater manufacturing enterprise of China commonly used is hot gas defrosting.This Defrost mode is divided into again two kinds of modes: hot gas bypass defrosting and reverse cycle defrosting.The former is that a part of gases at high pressure that compressor is discharged are directly bypassed to and in evaporimeter, carry out defrosting, now because the heat of high-pressure side refrigerant still comes from the heat that evaporimeter absorbs, when temperature is lower, defrosting is when fast not, there is no enough heat absorption, will cause system to be absorbed in protectiveness stopped status; The latter carries out reverse circulation defrosting by four-way change-over valve, now not only can not hot water preparing, and also can make original hot water energy scatter and disappear.More than can find out that more existing conventional Defrost modes have drawback separately.
The present invention is based on the problem proposing in above-mentioned background technology, designed a kind of new method that dehumidifies to prevent air source hot pump water heater frosting by binding soln.From above-mentioned background technology, can find out, current technology is all to defrost by different modes after the outdoor evaporimeter frosting of Teat pump boiler, the present invention considers from the thinking of pre-antifrost, the outdoor air that enters evaporimeter is carried out to pretreatment, its humidity is reduced, be suppressed at frosting in the heat transfer process of evaporimeter, strengthened outdoor evaporation and heat-exchange, improved the heating performance of system.Meanwhile, utilize the heat of heat pump circuit to carry out desorption and regeneration to solid absorbent, ensured stability and the high efficiency of dehumidifying and regenerative process.
Summary of the invention
Technical problem: the present invention is directed to the deficiency of current Defrost mode to air source hot pump water heater defrosting effect, proposed the system and method for a kind of solid dehumidifying prevention air source hot pump water heater frosting.
Summary of the invention: for solving the problems of the technologies described above, the system that the invention provides the frosting of a kind of solid dehumidifying prevention air source hot pump water heater, this system comprises: compressor, plate type heat exchanger, the first electric expansion valve, solid drier Coated Exchangers, gas-liquid separator, the second electric expansion valve, outdoor finned tube exchanger, pressure-reducing valve, water tank, water circulating pump, the first air-valve, the second air-valve, the 3rd air-valve, blower fan, block valve;
Heat pump and air circulation system when heat pump when this system is divided into dehumidifying and air circulation system, regeneration, wherein,
Heat pump when described dehumidifying:
Compressor comprises refrigerant inlet, the outlet of compressor is connected with the import of plate-type condenser, the first outlet of plate-type condenser is connected with the import of the first electric expansion valve, the outlet of the first electric expansion valve is connected with the first import of solid drier Coated Exchangers, the first outlet of solid drier Coated Exchangers is connected with the import of gas-liquid separator, the import of first outlet the second electric expansion valve of gas-liquid separator is connected, the outlet of the second electric expansion valve is connected with the import of outdoor finned-tube evaporator, the second outlet of gas-liquid separator is connected with the import of pressure-reducing valve, the first outlet of the outlet of pressure-reducing valve and outdoor finned-tube evaporator is connected with the import of compressor respectively,
Air circulation system when described dehumidifying:
The first air-valve is provided with air intake, the outlet of the first air-valve is connected with the second import of solid drier Coated Exchangers, the second outlet of solid drier Coated Exchangers is connected with the import of outdoor finned-tube evaporator, outdoor finned-tube evaporator second exports with the import of the 3rd air-valve and is connected, and the 3rd air-valve is provided with atmosphere outlet;
Heat pump when described regeneration comprises:
The outlet of compressor is connected with the import of plate-type condenser, the second outlet of plate-type condenser is connected with the import of block valve, the outlet of block valve is connected with the first import of solid drier Coated Exchangers, the first outlet of solid drier Coated Exchangers is connected with the import of gas-liquid separator, the import of first outlet the second electric expansion valve of gas-liquid separator is connected, the outlet of the second electric expansion valve is connected with the import of outdoor finned-tube evaporator, and the first outlet of outdoor finned-tube evaporator is connected with the import of compressor respectively; The first outlet of water tank is connected with the import of water circulating pump, and recirculated water delivery side of pump is connected with the import of plate-type condenser;
Air circulation system when described regeneration comprises:
Outdoor finned-tube evaporator second also exports and is connected with the import of the second air-valve, and the outlet of the second air-valve is connected with the second import of solid drier Coated Exchangers, and the second outlet of solid drier Coated Exchangers is connected with the import of outdoor finned-tube evaporator.
The present invention also provides the method for a kind of solid dehumidifying prevention air source hot pump water heater frosting, and the method comprises the steps:
Heat pump when described dehumidifying:
Gaseous refrigerant enter compressor compresses increasing temperature and pressure laggard enter plate-type condenser emit heat and be condensed into highly pressurised liquid, after entering afterwards the first electric expansion valve decrease temperature and pressure, enter solid drier Coated Exchangers absorption heat and evaporate a part of working medium, enter afterwards gas-liquid separator, the liquid of separating continues to enter after the second electric expansion valve throttling decrease temperature and pressure again in outdoor finned-tube evaporator heat absorption evaporation becomes the gas of low-temp low-pressure, out and through the gas of pressure-reducing valve be mixed into a loop of compressor formation with gas-liquid separator separates afterwards, meanwhile, the water in water tank is from one end by absorbing heat water circulating pump suction plate-type condenser, and the water after heating enters water tank from the other end and stores,
Air circulation system when described dehumidifying:
Outdoor humid air is entered in solid drier Coated Exchangers and is discharged moisture by the first air-valve, air after dehumidifying enters outdoor finned-tube evaporator release heat heating and cooling working medium, and the air that finally becomes low temperature and high relative humidity is turned back in atmosphere and gone by the 3rd air-valve;
Heat pump when described regeneration:
Gaseous refrigerant enter compressor compresses increasing temperature and pressure laggard enter plate-type condenser emit fraction heat and be cooled, enter release heat in solid drier Coated Exchangers by block valve afterwards and be condensed into highly pressurised liquid, enter heat absorption in the laggard external finned tube evaporimeter of entering the room of electric expansion valve throttling decrease temperature and pressure by gas-liquid separator and evaporate the gas that becomes low-temp low-pressure, enter compressor and form a loop; Meanwhile, the water in water tank passes through by natural flow from water tank one end that water circulating pump is laggard to be entered to absorb heat plate-type condenser, and the water after heating enters water tank from the other end and stores;
Air circulation system when described regeneration:
Enter solid drier Coated Exchangers from outdoor finned-tube evaporator Cryogenic air out through the second air-valve and become the circulated air of carrying superheated vapor, entering afterwards finned-tube evaporator cool-down dehumidification becomes Cryogenic air, then enters solid drier Coated Exchangers formation circulation by the second air-valve; The moisture wherein condensing in outdoor finned tube exchanger can be discharged system by condensate pipe.
Beneficial effect:
1. this system utilizes solid absorbent, to the absorption property of moisture, the humid air that enters evaporimeter is carried out to pretreatment, reduce the humidity of air, suppress the frosting problem of humid air at evaporator surface, prevented the problems such as the heating performance reduction that frosting problem is brought; Meanwhile, the heat of adsorption through the cold-producing medium of solid cladding heat exchanger in can absorption dehumidifying process, this part heat can be converted into condensation heat by system recoveries and for heat hot water;
2. this system utilizes heat pump fluid condensation liberated heat to carry out desorption to the moisture in solid, has not only ensured the stability of desorption process, and has recovered again the absorption property of solid; Meanwhile, the circulated air in regenerative process is carried superheated vapor heat release in evaporimeter of desorption, has reclaimed again system liberated heat by evaporimeter, has improved the regeneration efficiency of heat pump.
Brief description of the drawings
Fig. 1 is system architecture schematic diagram of the present invention.
Fig. 2 is heat pump circuit system schematic of the present invention.
Fig. 3 is adsorption process air circulation schematic diagram of the present invention.
Fig. 4 is desorption process air circulation schematic diagram of the present invention.
Compressor 1, plate type heat exchanger 2, the first electric expansion valve 3, solid drier Coated Exchangers 4, gas-liquid separator 13, the second electric expansion valve 5, outdoor finned tube exchanger 6, pressure-reducing valve 15, water tank 7, water circulating pump 8, the first air-valve 9, the second air-valve 10, the 3rd air-valve 11, blower fan 12, block valve 14.
Detailed description of the invention
Below in conjunction with drawings and the embodiments, patent of the present invention is described in further detail:
As Figure 1-4, the system of solid dehumidifying prevention air source hot pump water heater provided by the invention frosting, system comprises: compressor 1, plate type heat exchanger 2, the first electric expansion valve 3, solid drier Coated Exchangers 4, gas-liquid separator 13, the second electric expansion valve 5, outdoor finned tube exchanger 6, pressure-reducing valve 15, water tank 7, water circulating pump 8, the first air-valve 9, the second air-valve 10, the 3rd air-valve 11, blower fan 12, block valve 14.
Heat pump and air circulation system when heat pump when this system is divided into dehumidifying and air circulation system, regeneration, wherein,
Heat pump when described dehumidifying:
Compressor comprises refrigerant inlet, the outlet of compressor 1 is connected with the import of plate-type condenser 2, the first outlet of plate-type condenser 2 is connected with the import of the first electric expansion valve 3, the outlet of the first electric expansion valve 3 is connected with the first import of solid drier Coated Exchangers 4, the first outlet of solid drier Coated Exchangers 4 is connected with the import of gas-liquid separator 13, the import of first outlet the second electric expansion valve 5 of gas-liquid separator 13 is connected, the outlet of the second electric expansion valve 5 is connected with the import of outdoor finned-tube evaporator 6, the second outlet of gas-liquid separator 13 is connected with the import of pressure-reducing valve 15, the first outlet of the outlet of pressure-reducing valve 15 and outdoor finned-tube evaporator 6 is connected with the import of compressor 1 respectively.
Air circulation system when described dehumidifying:
The first air-valve 9 is provided with air intake, the outlet of the first air-valve 9 is connected with the second import of solid drier Coated Exchangers 4, the second outlet of solid drier Coated Exchangers 4 is connected with the import of outdoor finned-tube evaporator 6, outdoor finned-tube evaporator 6 second outlets are connected with the import of the 3rd air-valve 11, and the 3rd air-valve 11 is provided with atmosphere outlet.
Heat pump when described regeneration comprises:
The outlet of compressor 1 is connected with the import of plate-type condenser 2, the second outlet of plate-type condenser 2 is connected with the import of block valve 14, the outlet of block valve 14 is connected with the first import of solid drier Coated Exchangers 4, the first outlet of solid drier Coated Exchangers 4 is connected with the import of gas-liquid separator 13, the import of first outlet the second electric expansion valve 5 of gas-liquid separator 13 is connected, the outlet of the second electric expansion valve 5 is connected with the import of outdoor finned-tube evaporator 6, and the first outlet of outdoor finned-tube evaporator 6 is connected with the import of compressor 1 respectively; The first outlet of water tank 7 is connected with the import of water circulating pump 8, and the outlet of water circulating pump 8 is connected with the import of plate-type condenser 2.
Air circulation system when described regeneration comprises:
Outdoor finned-tube evaporator 6 second outlets are also connected with the import of the second air-valve 10, the outlet of the second air-valve 10 is connected with the second import of solid drier Coated Exchangers 4, and the second outlet of solid drier Coated Exchangers 4 is connected with the import of outdoor finned-tube evaporator 6.
The present invention also provides the method for a kind of solid dehumidifying prevention air source hot pump water heater frosting, and the method comprises the steps:
Heat pump when described dehumidifying:
Gaseous refrigerant enter compressor 1 compress increasing temperature and pressure laggard enter plate-type condenser 2 emit heat and be condensed into highly pressurised liquid, enter afterwards and enter solid drier Coated Exchangers 4 after the first electric expansion valve 3 decrease temperature and pressure and absorb heat and evaporate a part of working medium, enter afterwards gas-liquid separator 13, the liquid of separating continues to enter after the second electric expansion valve 5 throttlings decrease temperature and pressure again in outdoor finned-tube evaporator 6 heat absorption evaporation becomes the gas of low-temp low-pressure, the gas of separating and pass through pressure-reducing valve 15 with gas-liquid separator 13 is afterwards mixed into compressor 1 and forms a loop, meanwhile, the water in water tank 7 is from one end by absorbing heat water circulating pump 8 suction plate-type condensers 2, and the water after heating enters water tank from the other end and stores.
Air circulation system when described dehumidifying:
Outdoor humid air is entered in solid drier Coated Exchangers 4 and is discharged moisture by the first air-valve 9, air after dehumidifying enters outdoor finned-tube evaporator 6 release heat heating and cooling working medium, and the air that finally becomes low temperature and high relative humidity is turned back in atmosphere and gone by the 3rd air-valve 11.
Heat pump when described regeneration:
Gaseous refrigerant enter compressor 1 compress increasing temperature and pressure laggard enter plate-type condenser 2 emit fraction heat and be cooled, enter release heat in solid drier Coated Exchangers 4 by block valve 14 afterwards and be condensed into highly pressurised liquid, enter heat absorption in the laggard external finned tube evaporimeter 6 of entering the room of electric expansion valve 5 throttling decrease temperature and pressure by gas-liquid separator 13 and evaporate the gas that becomes low-temp low-pressure, enter compressor 1 and form a loop; Meanwhile, the water in water tank 7 passes through by natural flow from water tank one end that water circulating pump 8 is laggard to be entered to absorb heat plate-type condenser 2, and the water after heating enters water tank from the other end and stores.
Air circulation system when described regeneration:
Enter solid drier Coated Exchangers 4 from outdoor finned-tube evaporator 6 Cryogenic air out through the second air-valve 10 and become the circulated air of carrying superheated vapor, entering afterwards finned-tube evaporator 6 cool-down dehumidifications becomes Cryogenic air, then enters the 4 formation circulations of solid drier Coated Exchangers by the second air-valve 10; The moisture wherein condensing in outdoor finned tube exchanger 6 can be discharged system by condensate pipe.
The invention is characterized in the air loop of outdoor fin-tube heat exchanger and be provided with solid drier Coated Exchangers.
The specific embodiments of system of the present invention is as follows:
When dehumidifying operation, open air-valve 9 and air-valve 11, open water pump 8, close air-valve 10, close block valve 14, unlocking electronic expansion valve 3.When heat pump water heating, gaseous refrigerant through compressor 1 increasing temperature and pressure laggard enter condensation heat release in plate type heat exchanger 2, produce hot water, in solid drier Coated Exchangers 4, absorb heat and evaporate a part of cold-producing medium by entering after the first electric expansion valve 3 step-downs, the refrigerant liquid of separating by gas-liquid separator 13 afterwards enters after the second electric expansion valve 5 throttlings evaporation endothermic in the further laggard external finned tube formula evaporimeter 6 of entering the room of decrease temperature and pressure becomes the gaseous refrigerant of low-temp low-pressure, the gas of separating and pass through pressure-reducing valve 15 with gas-liquid separator 13 is afterwards mixed in compressor 1, complete heat pump cycle.Wherein, water pump 8 pumps into the water in water tank 7 in plate-type condenser 2 and absorbs heat, and the water after heating enters and stores from the other end of water tank 7; In air circulation, outdoor air enters solid drier Coated Exchangers 4, solid absorbent absorbs the moisture in humid air therein, air mass dryness fraction is improved, air after mass dryness fraction promotes enters release heat in outdoor finned-tube evaporator 6 becomes the air of low temperature and high relative humidity, gets back to outdoor afterwards by the 3rd air-valve 11.
When regeneration operation, open air-valve 10, close air-valve 9 and air-valve 11, switch off the pump 8, close electric expansion valve 3, open block valve 14.Gaseous refrigerant through compressor 1 increasing temperature and pressure laggard enter condensation emit sub-fraction heat and produce hot water in plate type heat exchanger 2, enter and in solid drier Coated Exchangers 4, continue release heat and be condensed into highly pressurised liquid by block valve 14 afterwards, enter evaporation endothermic in the laggard external finned tube formula evaporimeter 6 of entering the room of the second electric expansion valve 5 throttling decrease temperature and pressure through gas-liquid separator 13 afterwards, the refrigerant gas of last low-temp low-pressure enters in compressor again, completes heat pump cycle.Wherein, in water tank 7, entered in plate-type condenser 2 and absorbed heat by natural flow, the water after heating enters and stores from the other end of water tank 7; In air circulation, enter solid drier Coated Exchangers 4 from outdoor finned-tube evaporator Cryogenic air out by the second air-valve 10 and become the circulated air of carrying superheated vapor, air is cooled and dehumidifies in outdoor finned-tube evaporator 6 afterwards, and the moisture wherein condensing in outdoor finned tube evaporator 6 can be discharged system by condensate pipe.
The heat exchanger that utilization of the present invention has solid drier coating carries out pretreatment to the moisture in humid air, thereby in inhibition humid air, moisture is in the frosting of evaporator surface.The present invention utilizes solid absorbent coating to carry out dehumidification treatments to evaporator air, thereby significantly alleviates the frosting problem of Teat pump boiler, improves the heating performance of Teat pump boiler; After the moisture that solid absorbent absorbs reaches the limitation, utilize heat pump fluid condensation liberated heat to make the moisture desorption in solid absorbent, the superheated vapor that now circulated air is carried after desorption condenses in evaporator surface heat exchange, evaporimeter has been recycled again liberated heat in condenser, has improved the regeneration efficiency of heat pump.The present invention, by heat pump circuit in parallel and air circulation loop, has not only solved the problem of humid air in the easy frosting of evaporator surface, and has improved the efficiency of whole system water heating.
Claims (2)
1. a system for solid dehumidifying prevention air source hot pump water heater frosting, is characterized in that: this system comprises: compressor (1), plate type heat exchanger (2), the first electric expansion valve (3), solid drier Coated Exchangers (4), gas-liquid separator (13), the second electric expansion valve (5), outdoor finned tube exchanger (6), pressure-reducing valve (15), water tank (7), water circulating pump (8), the first air-valve (9), the second air-valve (10), the 3rd air-valve (11), blower fan (12), block valve (14);
Heat pump and air circulation system when heat pump when this system is divided into dehumidifying and air circulation system, regeneration, wherein,
Heat pump when described dehumidifying:
Compressor comprises refrigerant inlet, the outlet of compressor (1) is connected with the import of plate-type condenser (2), the first outlet of plate-type condenser (2) is connected with the import of the first electric expansion valve (3), the outlet of the first electric expansion valve (3) is connected with the first import of solid drier Coated Exchangers (4), the first outlet of solid drier Coated Exchangers (4) is connected with the import of gas-liquid separator (13), the import of first outlet the second electric expansion valve (5) of gas-liquid separator (13) is connected, the outlet of the second electric expansion valve (5) is connected with the import of outdoor finned-tube evaporator (6), the second outlet of gas-liquid separator (13) is connected with the import of pressure-reducing valve (15), the first outlet of the outlet of pressure-reducing valve (15) and outdoor finned-tube evaporator (6) is connected with the import of compressor (1) respectively,
Air circulation system when described dehumidifying:
The first air-valve (9) is provided with air intake, the outlet of the first air-valve (9) is connected with the second import of solid drier Coated Exchangers (4), the second outlet of solid drier Coated Exchangers (4) is connected with the import of outdoor finned-tube evaporator (6), outdoor finned-tube evaporator (6) second outlets are connected with the import of the 3rd air-valve (11), and the 3rd air-valve (11) is provided with atmosphere outlet;
Heat pump when described regeneration comprises:
The outlet of compressor (1) is connected with the import of plate-type condenser (2), the second outlet of plate-type condenser (2) is connected with the import of block valve (14), the outlet of block valve (14) is connected with the first import of solid drier Coated Exchangers (4), the first outlet of solid drier Coated Exchangers (4) is connected with the import of gas-liquid separator (13), the import of first outlet the second electric expansion valve (5) of gas-liquid separator (13) is connected, the outlet of the second electric expansion valve (5) is connected with the import of outdoor finned-tube evaporator (6), the first outlet of outdoor finned-tube evaporator (6) is connected with the import of compressor (1) respectively, the first outlet of water tank (7) is connected with the import of water circulating pump (8), and the outlet of water circulating pump (8) is connected with the import of plate-type condenser (2),
Air circulation system when described regeneration comprises:
Outdoor finned-tube evaporator (6) second outlets are also connected with the import of the second air-valve (10), the outlet of the second air-valve (10) is connected with the second import of solid drier Coated Exchangers (4), and the second outlet of solid drier Coated Exchangers (4) is connected with the import of outdoor finned-tube evaporator (6).
2. a method for solid dehumidifying prevention air source hot pump water heater frosting, is characterized in that: the method comprises the steps:
Heat pump when described dehumidifying:
Gaseous refrigerant enter compressor (1) compression increasing temperature and pressure laggard enter plate-type condenser (2) emit heat and be condensed into highly pressurised liquid, after entering afterwards the first electric expansion valve (3) decrease temperature and pressure, enter solid drier Coated Exchangers (4) absorption heat and evaporate a part of working medium, enter afterwards gas-liquid separator (13), the liquid of separating continues to enter after the second electric expansion valve (5) throttling decrease temperature and pressure again in outdoor finned-tube evaporator (6) heat absorption evaporation becomes the gas of low-temp low-pressure, the gas of separating and pass through pressure-reducing valve (15) with gas-liquid separator (13) is afterwards mixed into compressor (1) and forms a loop, meanwhile, the water in water tank (7) is from one end by absorbing heat water circulating pump (8) suction plate-type condenser (2), and the water after heating enters water tank from the other end and stores,
Air circulation system when described dehumidifying:
Outdoor humid air enters release moisture in solid drier Coated Exchangers (4) by the first air-valve (9), air after dehumidifying enters outdoor finned-tube evaporator (6) release heat heating and cooling working medium, and the air that finally becomes low temperature and high relative humidity is turned back in atmosphere and gone by the 3rd air-valve (11);
Heat pump when described regeneration:
Gaseous refrigerant enter compressor (1) compression increasing temperature and pressure laggard enter plate-type condenser (2) emit fraction heat and be cooled, enter release heat in solid drier Coated Exchangers (4) by block valve (14) afterwards and be condensed into highly pressurised liquid, enter heat absorption in the laggard external finned tube evaporimeter (6) of entering the room of electric expansion valve (5) throttling decrease temperature and pressure by gas-liquid separator (13) and evaporate the gas that becomes low-temp low-pressure, enter compressor (1) and form a loop; Meanwhile, the water in water tank (7) passes through by natural flow from water tank one end that water circulating pump (8) is laggard to be entered to absorb heat plate-type condenser (2), and the water after heating enters water tank from the other end and stores;
Air circulation system when described regeneration:
Enter solid drier Coated Exchangers (4) from outdoor finned-tube evaporator (6) Cryogenic air out through the second air-valve (10) and become the circulated air of carrying superheated vapor, entering afterwards finned-tube evaporator (6) cool-down dehumidification becomes Cryogenic air, then enters solid drier Coated Exchangers (4) formation circulation by the second air-valve (10); The moisture wherein condensing in outdoor finned tube exchanger (6) can be discharged system by condensate pipe.
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| CN105928290A (en) * | 2016-04-25 | 2016-09-07 | 江苏大学 | Adsorbing and frost restraining technology based refrigerating system of air-cooled refrigerator |
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| CN109974412A (en) * | 2019-04-29 | 2019-07-05 | 苏州达善净化科技有限公司 | A kind of dehumidifying energy-saving drying device and furnace drying method |
| CN109974412B (en) * | 2019-04-29 | 2023-11-03 | 苏州达善净化科技有限公司 | Dehumidifying energy-saving drying equipment and drying method |
| CN112880067A (en) * | 2021-01-22 | 2021-06-01 | 上海交通大学 | Adsorption type refrigeration and dehumidification combined system and method thereof |
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| CN113819508A (en) * | 2021-09-18 | 2021-12-21 | 西安交通大学 | Coupling power system with geothermal recovery function and operation method thereof |
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