CN105674452B - Air ejection humidification-membrane type combines desiccant cooling system with compression - Google Patents
Air ejection humidification-membrane type combines desiccant cooling system with compression Download PDFInfo
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- CN105674452B CN105674452B CN201610203009.1A CN201610203009A CN105674452B CN 105674452 B CN105674452 B CN 105674452B CN 201610203009 A CN201610203009 A CN 201610203009A CN 105674452 B CN105674452 B CN 105674452B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
- F24F1/0007—Indoor units, e.g. fan coil units
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
- F24F3/1417—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with liquid hygroscopic desiccants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/001—Compression cycle type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/0014—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using absorption or desorption
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/1435—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification comprising semi-permeable membrane
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/1458—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification using regenerators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2221/00—Details or features not otherwise provided for
- F24F2221/34—Heater, e.g. gas burner, electric air heater
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Drying Of Gases (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
The present invention relates to desiccant cooling field, especially air ejection humidification membrane types to combine desiccant cooling system with compression.Including membrane type dehumidification device, atomizer and injector, liquid inlet and liquid outlet is respectively set in the both ends of membrane type dehumidification device, fluid passage is connected between liquid inlet and liquid outlet, fluid passage outer surface coats hollow-fibre membrane, gas vent and gas access are respectively set on the inside of liquid inlet and liquid outlet, is connected by gas passage between gas access and gas vent；The gas access of membrane type dehumidification device and the outlet of wind turbine, the gas vent of membrane type dehumidification device are connected to the nozzle inlet of injector, and the Suction gas inlet of injector and the outlet of atomizer, the jet expansion of injector are connected to the air intake vent of fan coil.Water can be used as refrigeration working medium, air is directly cooled down, refrigeration effect is improved；Air suspension impurity is effectively avoided to greatly reduce system maintenance cost to the pollution of dehumidification solution simultaneously.
Description
Technical field
The present invention relates to desiccant cooling field, especially a kind of air ejection humidification-membrane type combines dehumidifying system with compression
Cooling system.
Background technology
The refrigeration system used at present is mainly compression, absorption, absorption type and steam-sprayed refrigeration system.On
The thermodynamics basic principle for stating refrigeration system is inverse Carnot cycle, chooses low boiling point refrigerant, binary solution etc. as refrigeration
Working medium realizes continuous refrigeration cycle by the endothermic process of refrigerant evaporation/desorption and the exothermic process of condensation/absorption.
Cooled working medium (water, air etc.), which exchanges heat in evaporator with refrigeration working medium, to cool down, and cold is obtained with this.
However, since the process that conventional refrigeration obtains cold carries out in evaporator, refrigerant and cooled working medium
Between existing heat transfer temperature difference can be inevitably generated irreversible heat loss.Meanwhile compression-type refrigerating system needs dedicated pressure
Contracting equipment, absorption, absorption type and steam-sprayed refrigeration system are due to heat transfer problem there are equipment volumes larger, Energy Efficiency Ratio
The problems such as low, is above very restricted in application.
In addition, the absorption air dehumidifier used at present is mainly lithium chloride solution dehumidification device, which makes
Purification must be filtered to air in, otherwise lithium chloride solution can be polluted, influence device performance.
Invention content
The purpose of the present invention is be directed to solve drawbacks described above existing in the prior art, it is proposed that a kind of air ejection adds
Wet-membrane type combines desiccant cooling system with compression, which can use water as refrigeration working medium, is directly cooled down to air,
Improve refrigeration effect；Pollution of the air suspension impurity to dehumidification solution is can effectively avoid simultaneously, greatly reduces system maintenance
Cost.
The technical scheme is that：A kind of air ejection humidification-membrane type combines desiccant cooling system with compression, including
Wind turbine, fan coil and compression refrigerating apparatus, wherein further include membrane type dehumidification device, atomizer and injector, membrane type dehumidifying dress
Liquid inlet and liquid outlet is respectively set in the both ends set, and fluid passage, liquid are connected between liquid inlet and liquid outlet
Channel outer surface coats hollow-fibre membrane, and being flowed in fluid passage has lithium-bromide solution, the inside of liquid inlet and liquid outlet
Gas vent and gas access is respectively set, is connected by gas passage between gas access and gas vent；
The gas access of membrane type dehumidification device and the outlet of wind turbine, the gas vent and injector of membrane type dehumidification device
Nozzle inlet connection, the Suction gas inlet of injector and the outlet of atomizer, the jet expansion and fan coil of injector
Air intake vent connection, membrane type dehumidification device includes regeneration sector；
Compression refrigerating apparatus includes evaporator, expansion valve, condenser and compressor, the outlet of injector and fan coil
Air intake vent is connected to, and the air outlet of fan coil is connected to the condensing fin port of condenser.
In the present invention, the fluid passage includes several precoated metal wire mesh tubes, and precoated metal wire mesh tube includes wire
Webmaster, woven wire tube outer surface are coated with hollow-fibre membrane.
The regeneration sector includes regenerator, and the liquid outlet of the membrane type dehumidification device passes through solution pump and regenerator
Entrance is connected to, and the wall surface of regenerator posts electric heating sheets, the liquid inlet of membrane type dehumidification device and the outlet of regenerator.It is molten
Lithium bromide weak solution after liquid pump will absorb vapor is constantly pumped into regenerator, so that solution temperature is increased by electric heating sheets,
Moisture evaporation, lithium-bromide solution becomes concentrated solution from weak solution, constantly regenerating, and dehumidification process is made to be carried out continuously.
Several baffle plates are arranged in interleaved in the gas passage.By the way that baffle plate is arranged, humid air is increased in
The contact area of empty fiber membrane, to reinforce mass transfer effect.
The entrance of atomizer is connected to liquid storage tank, and atomizer is by the water atomization in liquid storage tank.
The cooling water outlet of the fan coil is connected with the chilled water inlet of evaporator, the cooling water inlet of fan coil
It is connected with the chilled water outlet of evaporator, water system is made to constitute a set of water cycle, condenser between fan coil and evaporator
Water outlet be connected to the water inlet of evaporator by expansion valve, the outlet that the air intake of condenser passes through compressor and evaporator
Mouth connection.
Beneficial effects of the present invention：
(1) present invention uses injector as crucial refrigerating plant, and using water as refrigeration working medium, water is atomized in atomizer
And it is inhaled into injector, it is persistently evaporated in injector, directly absorbs the heat in air, such mode for obtaining cold avoids
Wall surface heat exchange, eliminates the irreversible heat loss caused by wall surface heat transfer temperature difference, avoid conventional refrigeration obtain it is cold
Irreversible heat loss caused by the wall surface heat exchange mode used when amount, therefore better refrigeration effect can be obtained；
(2) air dewetting is carried out using membrane type dehumidification device, membrane type dehumidification device is used using lithium bromide as dehumidification solution
Precoated metal wire mesh tube dehumidifies, and precoated metal wire mesh tube can avoid air suspension impurity while absorbing water vapor in air
Pollution to dehumidification solution, system are not necessarily to air filtration and purification apparatus, greatly reduce system maintenance cost.
Description of the drawings
Fig. 1 is air ejection humidification-membrane type desiccant cooling apparatus structure schematic diagram；
Fig. 2 is membrane type dehumidification device front view；
Fig. 3 is membrane type dehumidification device left view sectional view；
Fig. 4 is membrane type dehumidification device overhead sectional view；
Fig. 5 is air handling process psychrometric chart.
In figure：1 wind turbine；2 regenerators；3 atomizers；4 liquid storage tanks；5 solution pumps；6 membrane type dehumidification devices；7 injectors；8 wind
Machine coil pipe；9 evaporators；10 expansion valves；11 condensers；12 compressors；13 membrane type dehumidification device liquid inlets；14 membrane types dehumidifying dress
Set liquid outlet；15 precoated metal wire mesh tubes；16 membrane type dehumidification device gas accesses；17 membrane type dehumidification device gas vents；18
Baffle plate.
Specific implementation mode
The present invention is further illustrated with reference to the accompanying drawings and examples.
As shown in Figure 1, the air ejection humidification-membrane type desiccant cooling system include wind turbine 1, membrane type dehumidification device 6,
Injector 7, fan coil 8 and compression refrigerating apparatus.As shown in Figures 2 to 4, the membrane type dehumidification device 6 is internally provided with sky
Chamber, the both ends of membrane type dehumidification device 6 are respectively set liquid inlet 13 and liquid outlet 14, liquid inlet 13 and liquid outlet 14 it
Between be connected with fluid passage, the fluid passage includes more precoated metal wire mesh tubes 15, and precoated metal wire mesh tube 15 is with gold
Category wire mesh tube is base material, and woven wire tube outer surface coats hollow fiber film structure.Flowing has lithium-bromide solution in fluid passage.
The system uses lithium-bromide solution to be used as and removes wet absorption working medium.Hollow-fibre membrane is hydrophobic material, and the lithium-bromide solution in film exists
Leakage is not will produce in flowing, and the vapor in the outer humid air of film can penetrate hollow-fibre membrane and be brominated the suction of lithium solution
It receives.Gas vent 17 is arranged in the inside of liquid inlet 13, and gas access 16,16 He of gas access is arranged in the inside of liquid outlet 14
It is connected by gas passage between gas vent 17, several baffle plates 18 are arranged in interleaved in the gas passage, by setting
Baffle plate 18 is set, the contact area of humid air and hollow-fibre membrane is increased, to reinforce mass transfer effect.In membrane type dehumidification device,
Gas flow direction is opposite with liquid flow direction.
The gas access 16 of the membrane type dehumidification device 6 passes through the outlet of pipeline and wind turbine 1, membrane type dehumidification device 6
Gas vent 17 be connected to the nozzle inlet of injector 7 by pipeline；The liquid outlet 14 of membrane type dehumidification device 6 passes through solution
Pump 5 is connected to the entrance of regenerator 2, the outlet that the liquid inlet 13 of membrane type dehumidification device 6 passes through pipeline and regenerator 2.
Air a is inhaled into the gas passage of membrane type dehumidification device 6 under the action of wind turbine 1, and membrane type dehumidification device 6 uses lithium-bromide solution
As liquid desiccant, during gas passage flows, the vapor in air a through hollow-fibre membrane and is brominated air
The absorption of lithium solution dehumidifies, and vapor is become discharging heat during liquid from gaseous state, therefore from the gas of membrane type dehumidification device
The air of 17 outflow of body outlet is the air b of high temperature low humidity.Due to absorbing the moisture in air, the lithium-bromide solution after dehumidifying
Weak solution is become from concentrated solution.Weak solution is flowed out from the liquid outlet 14 of membrane type dehumidification device 6, and regenerator is pumped by solution pump 5
2, four peripheral wall surfaces of regenerator 2 post electric heating sheets, so that solution temperature is increased by electric heating sheets, moisture evaporation, and lithium bromide is molten
Liquid becomes concentrated solution from weak solution, and the liquid inlet 13 of membrane type dehumidification device 6, bromine are flowed by the liquid outlet of regenerator 2
Change lithium concentrated solution flows back to membrane type dehumidification device 6 and continues to dehumidify.
Lithium-bromide solution in humid air and film outside film can be selected by sexual isolation using hollow-fibre membrane, avoid air
Pollution of the suspended impurity to dehumidification solution, therefore dropped significantly without using air filtration and purification apparatus before the wind turbine 1 of the device
The system maintenance cost that low cleaning purifier generates.
The nozzle inlet of the injector 7 is connected to by pipeline with the gas vent 17 of membrane type dehumidification device 6, injector 7
Suction gas inlet by the outlet of pipeline and atomizer 3, the jet expansion of injector 7 passes through pipeline and fan coil 8
Air intake vent is connected to.The entrance of atomizer 3 is connected to liquid storage tank, and atomizer 3 is by the water atomization in liquid storage tank 4, membrane type dehumidification device 6
The air of middle blowout enters injector 7, and negative pressure is formed at nozzle, and water mist is sucked injector 7.Water mist is with air in injection
Contact is sufficiently mixed in the mixing chamber of device 7, water mist persistently evaporates and absorb heat, generates the humid air c of low temperature, and from injector
7 jet expansion discharge.The process obtains cold using the evaporation endothermic of water mist, avoids conventional refrigeration equipment in process of refrigerastion
It is middle because wall surface changes thermogenetic irreversible heat loss, therefore higher refrigeration effect can be obtained.
The compression refrigerating apparatus includes evaporator 9, expansion valve 10, condenser 11 and compressor 12.Fan coil 8 it is cold
But water out is connected with the chilled water inlet of evaporator 9, the chilled water outlet of the cooling water inlet and evaporator 9 of fan coil 8
It is connected, water system is made to constitute a set of water cycle between fan coil 8 and evaporator 9.The outlet of injector 7 passes through pipeline and wind
The air intake vent of machine coil pipe 8 is connected to, and the air outlet of fan coil 8 is connected to by pipeline with the condensing fin Single port of condenser 11.
The air being discharged from injector 7 enters fan coil 8 by pipeline, exchanges heat with the water at low temperature in fan coil 8.Further
Air d after cooling is blown out from fan coil 8.It heats up after the heat of water at low temperature absorption air in fan coil 8 and along pipeline
Into evaporator 9, evaporator 9 absorbs the heat of water at low temperature, so that water at low temperature is cooled down and flows into the cooling water of fan coil 8 along pipeline
Entrance.
Air d is blown to condenser, blows to the other end by one end of condenser 11, absorb simultaneously after the discharge of fan coil 8
The heat that condenser distributes water capacities heating treatment, the air e obtained after processing such as carries out and arranges to indoor environment.Condenser 11
Water outlet be connected to the water inlet of evaporator 9 by expansion valve 10, the air intake of condenser 11 passes through compressor 12 and evaporation
The gas outlet of device 9 is connected to.Refrigerant vapour in condenser 11 becomes liquid, high temperature and pressure system by after absorption heat from gaseous state
After cryogen is flowed by pipeline and expansion valve 10 in evaporator 9, the heat for the water at low temperature that evaporator 9 absorbs makes refrigerant be changed into
Refrigerant vapour, and high pressure steam is formed after being compressed by compressor 12, the gas access of condenser is entered along pipeline.Condense
Refrigerant in device absorbs the heat of the chilled water flowed out from fan coil 8 in evaporator 9, while refrigerant is in condenser
The wind that is blown out by fan coil 8 of heat dissipation absorb.
Working principle of the present invention is as follows described：Air a is inhaled into the gas of membrane type dehumidification device 6 under the action of wind turbine 1
Body channel, membrane type dehumidification device 6 are used as liquid desiccant using lithium-bromide solution, and the vapor in air a is through doughnut
Film is simultaneously brominated the absorption of lithium solution and dehumidifies, and vapor is become discharging heat during liquid from gaseous state, therefore is removed from membrane type
The air that the gas vent 17 of wet device flows out is the air b of high temperature low humidity.Solution pump 5 is by the lithium bromide after absorbing vapor
Weak solution is constantly pumped into regenerator 2 and is regenerated, and dehumidification process is made to be carried out continuously.After air b enters injector 7, at nozzle
Negative pressure is formed, water mist is sucked into injector 7, water mist is sufficiently mixed in the mixing chamber of injector 7 with air and contacts, and water mist is lasting
Heat is evaporated and absorbed, generates the humid air c of low temperature, and be discharged from the jet expansion of injector 7.Air c is entered by pipeline
Water at low temperature in fan coil 8, with fan coil 8 exchanges heat.Further the air d after cooling is blown out from fan coil 8.It is empty
Gas d blows to the other end, while the heat that absorptive condenser distributes after the discharge of fan coil 8 by one end of condenser 11, carries out
Etc. water capacities heating treatment, the air e obtained after processing arrange to indoor environment.
Claims (4)
1. a kind of air ejection humidification-membrane type combines desiccant cooling system, including wind turbine with compression（1）, fan coil（8）With
Compression refrigerating apparatus, it is characterised in that：It further include membrane type dehumidification device（6）, atomizer（3）And injector（7）, membrane type dehumidifying dress
It sets（6）Both ends liquid inlet is respectively set（13）And liquid outlet（14）, liquid inlet（13）And liquid outlet（14）Between
It is connected with fluid passage, fluid passage outer surface coats hollow-fibre membrane, and being flowed in fluid passage has lithium-bromide solution, liquid to enter
Mouthful（13）Inside be arranged gas vent（17）, liquid outlet（14）Inside be arranged gas access（16）, gas access（16）
And gas vent（17）Between connected by gas passage；
Membrane type dehumidification device（6）Gas access（16）With wind turbine（1）Outlet, membrane type dehumidification device（6）Gas go out
Mouthful（17）With injector（7）Nozzle inlet connection, injector（7）Suction gas inlet and atomizer（3）Outlet, injection
Device（7）Jet expansion and fan coil（8）Air intake vent connection, membrane type dehumidification device includes regeneration sector；
Compression refrigerating apparatus includes evaporator（9）, expansion valve（10）, condenser（11）And compressor（12）, fan coil（8）'s
Air outlet and condenser（11）Condensing fin port connection；
The fluid passage includes several precoated metal wire mesh tubes（15）, precoated metal wire mesh tube（15）Including metallic mesh tube,
Woven wire tube outer surface is coated with hollow-fibre membrane；
The regeneration sector is regenerator（2）, the membrane type dehumidification device（6）Liquid outlet（14）Pass through solution pump（5）With
Regenerator（2）Entrance connection, regenerator（2）Wall surface post electric heating sheets, membrane type dehumidification device（6）Liquid inlet（13）
With regenerator（2）Outlet.
2. air ejection humidification-membrane type according to claim 1 combines desiccant cooling system with compression, feature exists
In：Several baffle plates are arranged in interleaved in the gas passage（18）.
3. air ejection humidification-membrane type according to claim 1 combines desiccant cooling system with compression, feature exists
In：Atomizer（3）Entrance and liquid storage tank（4）Connection, atomizer（3）By liquid storage tank（4）In water atomization.
4. air ejection humidification-membrane type according to claim 1 combines desiccant cooling system with compression, feature exists
In：The fan coil（8）Cooling water outlet and evaporator（9）Chilled water inlet be connected, fan coil（8）Cooling water
Entrance and evaporator（9）Chilled water outlet be connected, condenser（11）Water outlet pass through expansion valve（10）With evaporator（9）'s
Water inlet is connected to, condenser（11）Air intake pass through compressor（12）With evaporator（9）Gas outlet connection.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610203009.1A CN105674452B (en) | 2016-03-31 | 2016-03-31 | Air ejection humidification-membrane type combines desiccant cooling system with compression |
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| CN201610203009.1A CN105674452B (en) | 2016-03-31 | 2016-03-31 | Air ejection humidification-membrane type combines desiccant cooling system with compression |
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| CN105674452A CN105674452A (en) | 2016-06-15 |
| CN105674452B true CN105674452B (en) | 2018-09-14 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107036191B (en) * | 2017-04-18 | 2023-02-14 | 中国海洋大学 | Cooling and dehumidifying combined air conditioning system with dehumidifier |
| CN111530200B (en) * | 2020-05-09 | 2022-03-08 | 宁波奥克斯电气股份有限公司 | Atomization device |
| KR20230018444A (en) * | 2020-05-31 | 2023-02-07 | 크레이튼 폴리머스 엘엘씨 | air cooling system |
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| CN105299784A (en) * | 2015-11-02 | 2016-02-03 | 西安交通大学 | Heat and mass recovery type solution membrane dehumidification system based on membrane distillation and dehumidification method |
| CN105333545A (en) * | 2015-11-20 | 2016-02-17 | 西安交通大学 | Heat pipe steam compression composite type refrigeration system for air conditioners and provided with ejector |
| CN205641294U (en) * | 2016-03-31 | 2016-10-12 | 中国海洋大学 | Air draws penetrates humidification - diaphragm type and compression refrigerating system that jointly dehumidifies |
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| CN105674452A (en) | 2016-06-15 |
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