CN101270899A - Solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner - Google Patents
Solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner Download PDFInfo
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- CN101270899A CN101270899A CNA2008100374146A CN200810037414A CN101270899A CN 101270899 A CN101270899 A CN 101270899A CN A2008100374146 A CNA2008100374146 A CN A2008100374146A CN 200810037414 A CN200810037414 A CN 200810037414A CN 101270899 A CN101270899 A CN 101270899A
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Abstract
A compact-type liquid dehumidification air conditioner in two-stage parallel connection which is driven by the solar energy comprises a two-stage dehumidification module, a regeneration module, a first evaporation cooling device, a cross flow heat exchanger and a second evaporation cooling device. The two-stage dehumidification module, the cross flow heat exchanger and two evaporation cooling devices constitute the upper layer of the solar compact type of liquid dehumidification air conditioner in two-stage parallel connection; the regeneration module constitutes the lower layer of the liquid dehumidification air conditioner. The modules are connected through the liquid pipeline or the air duct. Compared with the traditional liquid dehumidification air conditioner, the layered design of the air conditioner saves the space greatly; the parallel arrangement of the dehumidification module is convenient for the regulation of the gas and liquid flow ratio of each level; the operation with big concentration difference is in favor of the complete exertion of the liquid dehumidification capability, which realizes the energy storage and saving purpose. Therefore the compact-type liquid dehumidification air conditioner in two-stage parallel connection which is driven by the solar energy improves the deterioration of the dehumidification effect due to the gas liquid mixing heat during the dehumidification process.
Description
Technical field
The present invention relates to a kind of dehumidification air conditioner of Refrigeration Engineering technical field, specifically is a kind of solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner.
Background technology
Liquid dehumidifying air conditioner have can the independent process air advantage such as temperature and humidity, the driving of low temperature pyrogen.Compare with traditional central air-conditioning, its operating cost reduces by 40%, and control air humidity precision is higher, has avoided indoor cooling coil to coagulate the pollution that water brings, and has bactericidal effect, guarantees that IAQ is better.A kind of especially eco-friendly air conditioning mode of liquid dehumidifying air conditioner, no CFCS problem and the effect of literature and history effect can use low-grade heat sources such as solar energy, industrial wastewater to drive.
Present liquid dehumidifying air conditioner has the following disadvantages: 1) regeneration energy consumption height, 2) the accumulation of energy weak effect, 3) combine complex structure with heat pump etc.
Find through literature search prior art, patent (application) number is 02144128.6 Chinese patent " multistage method for dehumidifying liquid ", handle wind in this technology and pass through the multi-stage solution dehumidifying device successively, this technical pattern complexity, parts (pump) are many, power consumption is big, can not effectively control outlet air temperatures at different levels, can not guarantee the temperature regulating range of the air of needs.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, a kind of solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner is provided, make it utilize solar energy, adopt the two stage dehumidify module, the flexible modulation solution density, and effectively cool off air at inter-stage, effectively regulate the temperature and humidity of air.On structural configuration, realize the regeneration of dehumidifying and cooling and solution respectively in the levels of same casing, compact conformation, easy to use.
The present invention realizes by the following technical programs.The present invention includes: two stage dehumidify module, regeneration module, first evaporation-cooled device, cross-flow heat exchanger and second evaporation-cooled device.
Described two stage dehumidify module comprises: handle wind blower fan, the first packed tower module, the second packed tower module, solution cooling heat exchanger, first triple valve, first solution adjusting pump and second solution and regulate pump.
Described regeneration module comprises: regeneration wind blower fan, the 3rd packed tower module, auxiliary electrical heating module, solar thermal collector, second triple valve, the 3rd triple valve, concentrated solution liquid storing barrel, weak solution liquid storing barrel, main regenerative pump, auxiliary regenerative pump, first heat exchanger and regeneration air heat exchanger.
Described first evaporation-cooled device comprises: the 4th packed tower module and first water pump.
Described second evaporation-cooled device comprises: cooling air blower fan, the 5th packed tower module and second water pump.
Above-mentioned parts have constituted processing wind path gauge structure, regeneration wind path gauge structure, cooling air duct gauge structure, dehumidification solution path structure, the first water route path structure and the second water route path structure of air-conditioning of the present invention.
Described processing wind path gauge structure corresponding components connected mode is: handle the wind inlet pipe and be connected with processing wind blower fan inlet side, handling wind blower fan outlet side is connected with air intlet one side of the first packed tower module, air outlet slit one side of the first packed tower module is connected with cross-flow heat exchanger, cross-flow heat exchanger is connected with air intlet one side of the second packed tower module again, and air outlet slit one side of the second packed tower module is connected by the air inlet side of air channel with the 4th packed tower module.
Described regeneration wind path gauge structure corresponding components connected mode is: regeneration wind inlet pipe is connected with regeneration wind blower fan inlet side, regeneration wind blower fan outlet side is connected with the regeneration air heat exchanger, the regeneration air heat exchanger is connected with air intlet one side of the 3rd packed tower module again, and air outlet slit one side of the 3rd packed tower module is connected with the regeneration air heat exchanger by the air channel.
Described cooling air duct gauge structure corresponding components connected mode is: the cooling air inlet tube is connected with cooling air blower fan one side, cooling air blower fan opposite side is connected with air intlet one side of the 5th packed tower module, and air outlet slit one side of the 5th packed tower module is connected with cross-flow heat exchanger.
Described dehumidification solution path structure comprises solution dehumidification path and solution regeneration path.Described solution dehumidification path corresponding components connected mode is: the dehumidification solution pump inlet is connected with an outlet of concentrated solution fluid reservoir and the 3rd triple valve, the dehumidification solution delivery side of pump is connected with the solution cooling heat exchanger, and the solution cooling heat exchanger is connected with the second solution control valve with the first solution control valve.The first solution control valve opposite side is connected with the first packed tower solution module import, and the taphole of the first packed tower module is connected with the import of the 3rd triple valve.The second solution control valve opposite side is connected with the second packed tower solution module import, and the taphole of the second packed tower module is connected with the import of the 3rd triple valve.The opposite side outlet of the 3rd triple valve is connected with the weak solution liquid storing barrel.Described dehumidification solution regeneration path corresponding components connected mode is: the outlet of weak solution liquid storing barrel is connected with main regenerative pump import by the PPR pipe, main regeneration delivery side of pump is connected with first heat exchanger, an outlet of first heat exchanger and first triple valve converges, import with second triple valve is connected again, outlet of second triple valve is connected with the electrical auxiliary heater import, another outlet of second triple valve is connected with the solar thermal collector import, the electrical auxiliary heater outlet converges with the solar thermal collector outlet, be connected with the actified solution control valve, the actified solution control valve is connected with the 3rd packed tower module solution inlet port, the taphole of the 3rd packed tower module is connected with auxiliary regenerative pump import, auxiliary regeneration delivery side of pump is connected with the first triple valve import, outlet of first triple valve is connected with first heat exchanger, and first heat exchanger is connected with the concentrated solution fluid reservoir again.
The described first water route path structure corresponding components connected mode is: the taphole side of the 4th packed tower is connected with water inlet one side of first water pump, and water outlet one side of first water pump is connected with the solution inlet port side of the 4th packed tower.
The described second water route path structure corresponding components connected mode is: the taphole side of the 5th packed tower is connected with the import of solution cooling heat exchanger, the outlet side of solution cooling heat exchanger is connected with water inlet one side of second water pump, and water outlet one side of second water pump is connected with the solution inlet port side of the 5th packed tower.
Described cross-flow heat exchanger is the cross-flow heat exchanger of air and air heat exchange.
Described packed tower module is a kind of cuboid of being made by the PV plate, outsourcing thermal insulation layer, built-in spray thrower and the honeycomb curtain filler that wets, and there is filter screen at the air outlet slit place.Each interface before and after described packed tower module has up and down.Described upward lower interface is a solution channel, and described front and back interface is an air duct.
Described solar thermal collector is to be heat transfer medium with solution, is flat-plate collector, electron tubes type heat collector.
The basic functional principle of solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner: handle air successively through the first packed tower module, cross-flow heat exchanger, the second packed tower module, the 4th packed tower module, be subjected to pre-dehumidifying, cooling, dehumidifying, the processing of cooling more respectively, reach ventilation state.Dehumidification solution both can enter the first packed tower module once more after the first packed tower module and the second packed tower module dehumidify to air and the second packed tower module dehumidifies to air, also can enter the weak solution liquid storing barrel and wait regeneration.Thereby the big concentration difference that realizes solution changes the purpose that reaches accumulation of energy.Be the wettability power that guarantees that solution continues, the heat that adds of weak solution is mainly provided by solar thermal collector, and electrical heating is auxilliary.Actified solution can enter the 3rd packed tower module repeatedly and accept regeneration, thereby realizes big concentration difference recovery.Reach the purpose that reduces the regeneration energy consumption simultaneously.
With respect to prior art, the present invention has the following advantages: the big concentration difference running of (1) solution, and solution accumulation of energy ability is big; (2) overcome the negative effect that dehumidifying release heat-temperature raises and brings by cross-flow heat exchanger, effect on moisture extraction is good.(3) the bilevel layout of system, compact conformation, easily worn parts such as pump reduce.
Description of drawings
Fig. 1 is a kind of compact multi-level parallel connection liquid dehumidifying air conditioner of the present invention system architecture diagram
Fig. 2 is a packed tower structural representation of the present invention
Among the figure: the first packed tower module 1, the second packed tower module 2, the 4th packed tower module 3, cross-flow heat exchanger 4, the 3rd packed tower module 5, the 5th packed tower module 6, weak solution liquid storing barrel 7, handle wind blower fan 8, regeneration wind blower fan 9, cooling air blower fan 10, auxiliary electrical heating module 11, solar thermal collector 12, first heat exchanger 13, main regenerative pump 14, dehumidification solution pump 15, handle air channel 16, first water pump 17, the first solution control valve 18, the second solution control valve 19, actified solution control valve 20, concentrated solution liquid storing barrel 21, first triple valve 22, second water pump 23, thermal insulation layer 24, spray thrower 25, the honeycomb curtain filler 26 that wets, filter screen 27, sewage draining exit 28, regeneration air channel 29, regeneration air heat exchanger 30, second triple valve 31, the 3rd triple valve 32, first water route 33, second water route 34, solution cooling heat exchanger 35, dehumidification solution passage 36, auxiliary regenerative pump 37, cooling air air channel 38.
The specific embodiment
Below in conjunction with accompanying drawing embodiments of the invention are elaborated: present embodiment is being to implement under the prerequisite with the technical solution of the present invention, provided detailed embodiment and concrete operating process, but protection scope of the present invention is not limited to following embodiment.
As shown in Figure 1, present embodiment comprises the first packed tower module 1, the second packed tower module 2, the 4th packed tower module 3, cross-flow heat exchanger 4, the 3rd packed tower module 5, the 5th packed tower module 6, weak solution liquid storing barrel 7, handle wind blower fan 8, regeneration wind blower fan 9, cooling air blower fan 10, auxiliary electrical heating module 11, solar thermal collector 12, first heat exchanger 13, main regenerative pump 14, dehumidification solution pump 15, handle air channel 16, first water pump 17, the first solution control valve 18, the second solution control valve 19, actified solution control valve 20, concentrated solution liquid storing barrel 21, first triple valve 22, second water pump 23, regeneration air channel 29, regeneration air heat exchanger 30, second triple valve 31, the 3rd triple valve 32, first water route 33, second water route 34, solution cooling heat exchanger 35, dehumidification solution passage 36, auxiliary regenerative pump 37, cooling air air channel 38.
As shown in Figure 2, the packed tower module comprises thermal insulation layer 24, spray thrower 25, the wet curtain filler 26 of honeycomb, filter screen 27, sewage draining exit 28.
The structural configuration mode of described solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner is, the first packed tower module, the second packed tower module, cross-flow heat exchanger, the 4th packed tower module constitute the compaction type two-stage parallel connection liquid dehumidifying air conditioner upper strata, and the 3rd packed tower module, weak solution liquid storing barrel, concentrated solution liquid storing barrel and electrical auxiliary heater constitute liquid dehumidifying air conditioner lower floor.
Present embodiment comprises handles wind path gauge structure, regeneration wind path gauge structure, cooling air duct gauge structure, dehumidification solution path structure, the first water route path structure and the second water route path structure.Concrete connected mode is described as follows.
Described processing wind path gauge structure corresponding components connected mode is: handle air channel 16 and be connected with processing wind blower fan 8 inlet sides, handling wind blower fan 8 outlet sides is connected with air intlet one side of the first packed tower module 1, air outlet slit one side of the first packed tower module 1 is connected with cross-flow heat exchanger 4, cross-flow heat exchanger 4 is connected with air intlet one side of the second packed tower module 2 again, and air outlet slit one side of the second packed tower module 2 is connected by the air inlet side of air channel with the 4th packed tower module 3.
Described regeneration wind path gauge structure corresponding components connected mode is: regeneration wind air channel 29 is connected with regeneration wind blower fan 9 inlet sides, regeneration wind blower fan 9 outlet sides are connected with regeneration air heat exchanger 30, regeneration air heat exchanger 30 is connected with air intlet one side of the 5th packed tower module 5 again, and air outlet slit one side of the 3rd packed tower module 5 is connected with regeneration air heat exchanger 30 by the air channel.
Described cooling air duct gauge structure corresponding components connected mode is: cooling air air channel 38 is connected with cooling air blower fan 10 1 sides, cooling air blower fan 10 opposite sides are connected with air intlet one side of the 5th packed tower module 6, and air outlet slit one side of the 5th packed tower module 6 is connected with cross-flow heat exchanger 2.
Described dehumidification solution path structure comprises solution dehumidification path and solution regeneration path.Described solution dehumidification path corresponding components connected mode is: 15 imports of dehumidification solution pump are connected with an outlet of concentrated solution fluid reservoir and the 3rd triple valve 32 by pvc pipe, the outlet of dehumidification solution pump 15 is connected with solution cooling heat exchanger 35, and solution cooling heat exchanger 35 is connected with the second solution control valve 19 with the first solution control valve 18 by pvc pipe.The first solution control valve, 18 opposite sides are connected with 1 import of the first packed tower solution module, and the taphole of the first packed tower module 1 is connected with the import of the 3rd triple valve 32.The second solution control valve, 19 opposite sides are connected with 2 imports of the second packed tower solution module, and the taphole of the second packed tower module 2 is connected with the import of the 3rd triple valve 32.The opposite side outlet of the 3rd triple valve 32 is connected with weak solution liquid storing barrel 7.Described dehumidification solution regeneration path corresponding components connected mode is: the outlet of weak solution liquid storing barrel 7 is connected with main regenerative pump 14 imports by the PPR pipe, the outlet of main regenerative pump 14 is connected with first heat exchanger 13, an outlet of first heat exchanger 13 and first triple valve 22 converges, import with second triple valve 31 is connected again, 31 1 outlets of second triple valve are connected with electrical auxiliary heater 11 imports, another outlet of second triple valve 31 is connected with solar thermal collector 12 imports, electrical auxiliary heater 11 outlets converge with solar thermal collector 12 outlets, be connected with actified solution control valve 20, actified solution control valve 20 is connected with the 3rd packed tower module 5 solution inlet port, the taphole of the 3rd packed tower module 5 is connected with auxiliary regenerative pump 37 imports, the outlet of auxiliary regenerative pump 37 is connected with 22 imports of first triple valve, 22 1 outlets of first triple valve are connected with first heat exchanger 13, and first heat exchanger 13 is connected with concentrated solution fluid reservoir 21 again.
The described first water route path structure corresponding components connected mode is: the taphole side by PVC water pipe the 4th packed tower 3 is connected with water inlet one side of first water pump 17, and water outlet one side of first water pump 17 is connected with the solution inlet port side of the 4th packed tower 3.
The described second water route path structure corresponding components connected mode is: the taphole side by PVC water pipe the 5th packed tower 6 is connected with 35 imports of solution cooling heat exchanger, the outlet side of solution cooling heat exchanger 35 is connected with water inlet one side of second water pump 23, and water outlet one side of second water pump 23 is connected with the solution inlet port side of the 5th packed tower 6.
The cool-down dehumidification mode of the two-stage liquid desiccant air conditioning of being realized by the said equipment is: (outdoor air or indoor and outdoor are mixed wind to handle air, be called for short and handle air) enter blower fan by handling wind air channel 16 inlets, enter the first packed tower module 1 then, airborne moisture is absorbed by dehumidification solution, discharge heat, the temperature of air raises.If continue dehumidifying, then effect on moisture extraction is with variation.Therefore this processing air then enters cross-flow heat exchanger 2, heat is passed to the cooling air of heat exchanger opposite side.Fallen warm air then and entered the second packed tower module 3 again, airborne steam is that dehumidification solution further absorbs, and becomes the lower air of water capacity.Equally, follow the transfer of moisture, the temperature of air can raise.Last air enters the 4th packed tower module 4, and the part water evaporates is in air, and air themperature descends, thereby reaches comfortable air-supply humidity operating mode.
The present invention compares with traditional liquid dehumidifying air conditioner, and the hierarchical design of this air-conditioning has been saved the space greatly, The convenient gas-liquid flow-rate ratio at different levels that is arranged in parallel of dehumidification module is regulated, and big concentration difference operation is conducive to fully send out Wave the dehumidifying effect of solution, realize accumulation of energy and energy-conservation purpose. Dehumidification module two inter-stage devaporizers and The introducing of cross-flow heat exchanger takes full advantage of natural cooling source cooling processing air, thereby has improved in the dehumidification process The deterioration of the effect on moisture extraction that gas-liquid mixed heat causes. Use two stage dehumidify packed tower module, a regeneration is filled out Material tower module in conjunction with cross-flow heat exchanger and evaporative cooling packed tower module, mainly relies on solar thermal collector to do Be thermal source. This equipment can be used for the air conditioning of the occasions such as commercial building, civil buildings.
Claims (6)
1, a kind of solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioner, comprising: two stage dehumidify module, regeneration module, first evaporation-cooled device, cross-flow heat exchanger and second evaporation-cooled device is characterized in that:
Described two stage dehumidify module comprises: handle wind blower fan, the first packed tower module, the second packed tower module, solution cooling heat exchanger, first triple valve, first solution adjusting pump and second solution and regulate pump;
Described regeneration module comprises: regeneration wind blower fan, the 3rd packed tower module, auxiliary electrical heating module, solar thermal collector, second triple valve, the 3rd triple valve, concentrated solution liquid storing barrel, weak solution liquid storing barrel, main regenerative pump, auxiliary regenerative pump, first heat exchanger and regeneration air heat exchanger;
Described first evaporation-cooled device comprises: the 4th packed tower module and first water pump;
Described second evaporation-cooled device comprises: cooling air blower fan, the 5th packed tower module and second water pump;
Above-mentioned parts have constituted processing wind path gauge structure, regeneration wind path gauge structure, cooling air duct gauge structure, dehumidification solution path structure, the first water route path structure and the second water route path structure, wherein:
Described processing wind path gauge structure is: handle the wind inlet pipe and be connected with processing wind blower fan inlet side, handling wind blower fan outlet side is connected with air intlet one side of the first packed tower module, air outlet slit one side of the first packed tower module is connected with cross-flow heat exchanger, cross-flow heat exchanger is connected with air intlet one side of the second packed tower module again, and air outlet slit one side of the second packed tower module is connected by the air inlet side of air channel with the 4th packed tower module;
Described regeneration wind path gauge structure is: regeneration wind inlet pipe is connected with regeneration wind blower fan inlet side, regeneration wind blower fan outlet side is connected with the regeneration air heat exchanger, the regeneration air heat exchanger is connected with air intlet one side of the 3rd packed tower module again, and air outlet slit one side of the 3rd packed tower module is connected with the regeneration air heat exchanger by the air channel;
Described cooling air duct gauge structure is: the cooling air inlet tube is connected with cooling air blower fan one side, and cooling air blower fan opposite side is connected with air intlet one side of the 5th packed tower module, and air outlet slit one side of the 5th packed tower module is connected with cross-flow heat exchanger;
Described dehumidification solution path structure is: the dehumidification solution pump inlet is connected with an outlet of concentrated solution fluid reservoir and the 3rd triple valve, the dehumidification solution delivery side of pump is connected with the solution cooling heat exchanger, the solution cooling heat exchanger is connected with the second solution control valve with the first solution control valve, the first solution control valve opposite side is connected with the first packed tower solution module import, the taphole of the first packed tower module is connected with the import of the 3rd triple valve, the second solution control valve opposite side is connected with the second packed tower solution module import, the taphole of the second packed tower module is connected with the import of the 3rd triple valve, and the opposite side outlet of the 3rd triple valve is connected with the weak solution liquid storing barrel;
The outlet of weak solution liquid storing barrel is connected with main regenerative pump import, main regeneration delivery side of pump is connected with first heat exchanger, an outlet of first heat exchanger and first triple valve converges, import with second triple valve is connected again, outlet of second triple valve is connected with the electrical auxiliary heater import, another outlet of second triple valve is connected with the solar thermal collector import, the electrical auxiliary heater outlet converges with the solar thermal collector outlet, be connected with the actified solution control valve, the actified solution control valve is connected with the 3rd packed tower module solution inlet port, the taphole of the 3rd packed tower module is connected with auxiliary regenerative pump import, auxiliary regeneration delivery side of pump is connected with the first triple valve import, outlet of first triple valve is connected with first heat exchanger, and first heat exchanger is connected with the concentrated solution fluid reservoir again;
The described first water route path structure is: the taphole side of the 4th packed tower is connected with water inlet one side of first water pump, and water outlet one side of first water pump is connected with the solution inlet port side of the 4th packed tower;
The described second water route path structure is: the taphole side of the 5th packed tower is connected with the import of solution cooling heat exchanger, the outlet side of solution cooling heat exchanger is connected with water inlet one side of second water pump, and water outlet one side of second water pump is connected with the solution inlet port side of the 5th packed tower.
2, solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioner according to claim 1 is characterized in that, described cross-flow heat exchanger is the cross-flow heat exchanger of air and air heat exchange.
3, solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioner according to claim 1 is characterized in that, described packed tower module is a kind of cuboid, outsourcing thermal insulation layer, built-in spray thrower and the honeycomb curtain filler that wets, and there is filter screen at the air outlet slit place.
4, according to claim 1 or 3 described solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioners, it is characterized in that each interface before and after described packed tower module has up and down.
5, solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioner according to claim 4 is characterized in that, described upward lower interface is a solution channel, and described front and back interface is an air duct.
6, solar energy driving compaction type plural parallel stage liquid dehumidifying air conditioner according to claim 1 is characterized in that, described solar thermal collector is to be heat transfer medium with solution, is flat-plate collector, electron tubes type heat collector.
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2008100374146A CN100554796C (en) | 2008-05-15 | 2008-05-15 | Solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner |
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| CNB2008100374146A CN100554796C (en) | 2008-05-15 | 2008-05-15 | Solar energy driving compaction type two-stage parallel connection liquid dehumidifying air conditioner |
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| CN100554796C CN100554796C (en) | 2009-10-28 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103047724A (en) * | 2013-01-11 | 2013-04-17 | 上海交通大学 | Multi-energy complementally driven dehumidification air-conditioning system |
| CN103185379A (en) * | 2013-03-29 | 2013-07-03 | 江苏大学 | Novel solar energy liquid dehumidifying air-conditioning system and implementation method |
| CN103791576A (en) * | 2014-02-17 | 2014-05-14 | 东南大学 | Low-grade heat source drive solution temperature changing two-stage solution dehumidification air conditioner |
| CN104061634A (en) * | 2014-03-14 | 2014-09-24 | 东南大学 | Two-stage high and low temperature liquid desiccant air-conditioning system driven by heat pump and controlling method |
| CN115164293A (en) * | 2022-06-08 | 2022-10-11 | 东南大学 | Air dehumidifying device based on solar interface evaporation regeneration |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4222244A (en) * | 1978-11-07 | 1980-09-16 | Gershon Meckler Associates, P.C. | Air conditioning apparatus utilizing solar energy and method |
| US4205529A (en) * | 1978-12-04 | 1980-06-03 | The United States Of America As Represented By The United States Department Of Energy | LiCl Dehumidifier LiBr absorption chiller hybrid air conditioning system with energy recovery |
-
2008
- 2008-05-15 CN CNB2008100374146A patent/CN100554796C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103047724A (en) * | 2013-01-11 | 2013-04-17 | 上海交通大学 | Multi-energy complementally driven dehumidification air-conditioning system |
| CN103047724B (en) * | 2013-01-11 | 2015-01-14 | 上海交通大学 | Multi-energy complementally driven dehumidification air-conditioning system |
| CN103185379A (en) * | 2013-03-29 | 2013-07-03 | 江苏大学 | Novel solar energy liquid dehumidifying air-conditioning system and implementation method |
| CN103185379B (en) * | 2013-03-29 | 2015-01-07 | 江苏大学 | Novel solar energy liquid dehumidifying air-conditioning system and implementation method |
| CN103791576A (en) * | 2014-02-17 | 2014-05-14 | 东南大学 | Low-grade heat source drive solution temperature changing two-stage solution dehumidification air conditioner |
| CN103791576B (en) * | 2014-02-17 | 2016-04-06 | 东南大学 | A kind of low-grade heat source drives and becomes solution temperature two-stage liquid desiccant air conditioning |
| CN104061634A (en) * | 2014-03-14 | 2014-09-24 | 东南大学 | Two-stage high and low temperature liquid desiccant air-conditioning system driven by heat pump and controlling method |
| CN104061634B (en) * | 2014-03-14 | 2016-11-02 | 东南大学 | A kind of heat pump driven two-stage high/low temperature solution dehumidifying air-conditioning system and control method |
| CN115164293A (en) * | 2022-06-08 | 2022-10-11 | 东南大学 | Air dehumidifying device based on solar interface evaporation regeneration |
| CN115164293B (en) * | 2022-06-08 | 2023-09-05 | 东南大学 | Air dehumidifying device based on solar energy interface evaporation regeneration |
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| CN100554796C (en) | 2009-10-28 |
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