CN202955793U - Heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system - Google Patents
Heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system Download PDFInfo
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- CN202955793U CN202955793U CN 201220565530 CN201220565530U CN202955793U CN 202955793 U CN202955793 U CN 202955793U CN 201220565530 CN201220565530 CN 201220565530 CN 201220565530 U CN201220565530 U CN 201220565530U CN 202955793 U CN202955793 U CN 202955793U
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Abstract
A heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system comprises a new air heat recycling heat-humidity exchange core component and a return air heat recycling heat-humidity exchange core component. The new air heat recycling heat-humidity exchange core component comprises at least one new air heat recycling heat-humidity exchange cores. Each new air heat recycling heat-humidity exchange core is provided with an air inlet at the bottom and an air outlet at the top. The air inlet of each one new air heat recycling heat-humidity exchange core is serially connected with the air outlet of the other new air heat recycling heat-humidity exchange core through an air pipe to form a new air heat recycling heat-humidity exchange passage. A first solution groove is arranged below each new air heat recycling heat-humidity exchange core. The heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system is efficient in dehumidifying, high in total heat recycling, compact in structure, low in manufacturing cost, small in size, and applicable to small office buildings, serviced apartments, villas and common residences.
Description
Technical field
The utility model relates to a kind of solution-type air processor, especially relates to the solution humidifying air-conditioning system that a kind of heat pump drives the wet exchange of refluent heat, belongs to the damping field of air conditioning, especially solution-type air processor field.
Background technology
The solution humidifying air-conditioning system, owing to can utilizing low-grade energy, saving many many-sided advantages such as energy resource consumption, protection of the environment, has obtained paying close attention to comparatively widely in recent years.In existing solution humidifying air-conditioning system, what at present technology comparative maturity, range of application were wider is distributary heat insulation-type solution humidifying air-conditioning system, yet, dehumidification rate, the total heat recovery efficiency of distributary heat insulation-type solution humidifying air-conditioning system are lower, and set structure complexity, cost is high, bulky, is not suitable for the projects such as little space buildings and house.
The utility model content
The purpose of this utility model is to provide a kind of dehumidification rate, total heat recovery efficiency high, compact conformation, cost is low, and volume is little, and the heat pump that can be used in small-sized storied office building, apartment with hotel-styled services, villa and ordinary residence drives the solution humidifying air-conditioning system of the wet exchange of refluent heat.
Heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, comprise that new wind-heat reclaims heat wet exchange core component and return air heat reclaims the wet exchange of heat core component, wind-heat reclaims the wet exchange of heat core component and comprises that more than one new wind-heat reclaims the wet exchange of heat core body, the bottom that each new wind-heat reclaims the wet exchange of heat core body has respectively air inlet, the top that each new wind-heat reclaims the wet exchange of heat core body has respectively air outlet, the air outlet of the air inlet of the wet exchange of a new wind-heat recovery heat core body and the wet exchange of another new wind-heat recovery heat core body is mutually connected and is linked to be a hot wet interchange channel of new wind-heat recovery by airduct, the below that each new wind-heat reclaims the wet exchange of heat core body is respectively equipped with the first solution tank, the bottom of each the first solution tank is connected with the water inlet of the first solution water-supply-pipe respectively, the middle part of each the first solution water-supply-pipe is in series with respectively the first solution circulation pump, the delivery port of each the first solution water-supply-pipe is connected with the water injector that is arranged on the wet exchange of return air heat recovery heat core body internal upper part,
Described return air heat reclaims the wet exchange of heat core component and comprises that more than one return air heat reclaims the wet exchange of heat core body, the bottom that each return air heat reclaims the wet exchange of heat core body has respectively air inlet, the top that each return air heat reclaims the wet exchange of heat core body has respectively air outlet, the air outlet of the air inlet of the wet exchange of a return air heat recovery heat core body and the wet exchange of another return air heat recovery heat core body is mutually connected and is linked to be a hot wet interchange channel of return air heat recovery by airduct, the below that each return air heat reclaims the wet exchange of heat core body is respectively equipped with the second solution tank, the bottom of each the second solution tank is connected with the water inlet of the second solution water-supply-pipe respectively, the middle part of each the second solution water-supply-pipe is in series with respectively the second solution circulation pump, the delivery port of each the second solution water-supply-pipe is connected with the water injector that is arranged on the wet exchange of new wind-heat recovery heat core body internal upper part,
The air outlet that described new wind-heat reclaims the wet exchange of heat core component is connected with the air inlet of Dehumidifying element heat exchange core body assembly by pipeline, Dehumidifying element heat exchange core body assembly comprises more than one Dehumidifying element heat exchange core body, the bottom of each Dehumidifying element heat exchange core body has respectively air inlet, the top of each Dehumidifying element heat exchange core body has respectively air outlet, the air outlet of the air inlet of a Dehumidifying element heat exchange core body and another Dehumidifying element heat exchange core body is mutually connected and is linked to be a dehumidifying heat exchanger channels by airduct, the below of each Dehumidifying element heat exchange core body is respectively equipped with the 3rd solution tank, the bottom of each the 3rd solution tank is connected with the water inlet of the 3rd solution water-supply-pipe respectively, the middle part of each the 3rd solution water-supply-pipe is in series with respectively the outer circulation path of the 3rd solution circulation pump and vaporation-type plate type heat exchanger, the delivery port of each the 3rd solution circulation pump is connected with the water injector that is arranged on Dehumidifying element heat exchange core body internal upper part,
The air outlet that described return air heat reclaims the wet exchange of heat core component is connected with the air inlet of regeneration unit heat exchange core body assembly by pipeline, regeneration unit heat exchange core body assembly comprises more than one regeneration unit heat exchange core body, the bottom of each regeneration unit heat exchange core body has respectively air inlet, the top of each regeneration unit heat exchange core body has respectively air outlet, the air outlet of the air inlet of a regeneration unit heat exchange core body and another regeneration unit heat exchange core body is mutually connected and is linked to be a regeneration passage by airduct, the below of each regeneration unit heat exchange core body is respectively equipped with the 4th solution tank, the bottom of each the 4th solution tank is connected with the water inlet of the 4th solution water-supply-pipe respectively, the middle part of each the 4th solution water-supply-pipe is in series with respectively the outer circulation path of the 4th solution circulation pump and condensing plate type heat exchanger, the delivery port of each the 4th solution circulation pump is connected with the water injector that is arranged on regeneration unit heat exchange core body internal upper part,
The outlet of the refrigerant circulation path in each described vaporation-type plate type heat exchanger is connected with the entrance of compressor by pipeline, the outlet of compressor is connected by the entrance of the refrigerant circulation path of the described condensing plate type heat exchanger of pipeline and each, the outlet of the refrigerant circulation path of each described condensing plate type heat exchanger is connected with the entrance of expansion valve by pipeline, and the outlet of expansion valve is connected by the entrance of the refrigerant circulation path of the described vaporation-type plate type heat exchanger of pipeline and each;
The delivery port of each described the 3rd solution tank bottom is connected with the water inlet of the left heat exchanger channels of plate type heat exchanger by the 3rd solution flow pipe road that is in series with the 3rd solution water-delivery pump respectively, and the delivery port of the left heat exchanger channels of this plate type heat exchanger is connected with the water inlet of described the 4th solution tank;
The delivery port of each described the 4th solution tank bottom is connected with the water inlet of the right heat exchanger channels of described plate type heat exchanger by the 4th solution flow pipe road that is in series with the 4th solution water-delivery pump respectively, and the delivery port of the right heat exchanger channels of this plate type heat exchanger is connected with the water inlet of described the 3rd solution tank;
Each described the 4th solution tank is connected with the delivery port of filling pipe, is in series with pipe valve or water compensating valve on filling pipe.
Heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, the quantity that wherein said new wind-heat reclaims the wet exchange of heat core body, the wet exchange of described return air heat recovery heat core body, described Dehumidifying element heat exchange core body, described regeneration unit heat exchange core body, described the first solution tank, described the second solution tank, described the 3rd solution tank, described the 4th solution tank is all 2 or 3 or 4 or 5 or 6, and the quantity of described compressor and described expansion valve is 2 or 3 or 4 or 5 or 6.
With existing solution dehumidification unit, compare, heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat to have the following advantages:
1, dehumidifying and heat recycle process Energy Efficiency Ratio are higher.Because dehumidifying, the wet exchange of regenerated heat core body adopt the wet exchanging form form of refluent heat, and the wet exchanging form of refluent heat generally exceeds more than 30% than the wet exchanging form efficiency of damp and hot exchanging of existing distributary heat, therefore, heat pump of the present utility model drives the solution humidifying air-conditioning system dehumidification rate of the wet exchange of refluent heat, higher than the dehumidification rate of existing distributary heat insulation-type solution humidifying air-conditioning system.In addition, the wet exchange of the full recuperation of heat heat core body in the utility model adopts the refluent heat exchanging form that wets equally, therefore total heat recovery efficiency is higher than the full recuperation of heat of distributary.Comprehensively known, dehumidifying of the present utility model and heat recycle process are more energy-conservation.
2, unit operation is more stable, reliable.Because the wet exchange of full recuperation of heat heat core body adopts the wet exchanging form heat exchanger effectiveness of refluent heat, than the wet exchanging form efficiency of damp and hot exchanging of traditional distributary heat, exceed more than 30%, wet and exchange the energy that greatly reduces new wind by heat, therefore reduced the load of solution dehumidification unit, the condensing pressure of guaranteeing heat pump refrigeration system be controlled at can the scope of stable operation in.
3, set structure compactness, the machine packet size is little, and efficiency is high, is applicable to the projects such as little space buildings and house.At present existing solution humidifying air-conditioning system air quantity is only applicable to very greatly large-scale Gongjian, yet along with the fast rise of the energy consumptions such as residential houses, small-sized Gongjian, therefore the demand of little air quantity unit is seemed to very urgent.It is compact not that but existing new blower fan group has structure, the drawbacks such as efficiency is low, and the utility model has overcome these drawbacks, be of compact construction, and because utilizing the adverse current form to improve efficiency of damp and hot exchanging, thereby make small solution damping unit there is the advantages such as compact conformation, the machine packet size is little, efficiency is high, can be widely used in small-sized storied office building, hotel apartment, villa, ordinary residence having the new wind in the occasion, particularly humiture independence control air conditioner system of new wind damping demand to process.
In sum, heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, except thering are all characteristics such as high runnability, low energy expenditure, high air quality, utilized the reverse-flow gas-liquid direct contact heat Switching Module that wets, improved efficiency of damp and hot exchanging, also there is compact conformation, volume is little, air quantity is little, performance is high and is applicable to the characteristics of the projects such as small-sized storied office building, apartment with hotel-styled services, house.In a word, the solution humidifying air-conditioning system that heat pump of the present utility model drives the wet exchange of refluent heat to improving the air-conditioning system runnability, reduce energy resource consumption, improve solution humidifying air-conditioning system that air quality and heat pump drive the wet exchange of refluent heat in the application of small-sized storied office building, apartment with hotel-styled services and Housing Project etc., significant.
Below in conjunction with accompanying drawing, the technical solution of the utility model is described further.
The accompanying drawing explanation
Fig. 1 is the fundamental diagram that heat pump of the present utility model drives a kind of embodiment of the wet solution humidifying air-conditioning system exchanged of refluent heat;
Fig. 2 is the fundamental diagram that heat pump of the present utility model drives the another kind of embodiment of the wet solution humidifying air-conditioning system exchanged of refluent heat;
Fig. 3 is the fundamental diagram that heat pump of the present utility model drives another embodiment of the wet solution humidifying air-conditioning system exchanged of refluent heat.
The specific embodiment
As shown in Figure 1, heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, comprise that new wind-heat reclaims heat wet exchange core component and return air heat reclaims the wet exchange of heat core component, wind-heat reclaims the wet exchange of heat core component and comprises that a new wind-heat reclaims the wet exchange of heat core body 1, the bottom that new wind-heat reclaims the wet exchange of heat core body 1 has air inlet, the top that new wind-heat reclaims the wet exchange of heat core body 1 has air outlet, the below that new wind-heat reclaims the wet exchange of heat core body 1 is provided with the first solution tank 2, the bottom of the first solution tank 2 is connected with the water inlet of the first solution water-supply-pipe 3, the middle part of the first solution water-supply-pipe 3 is in series with the first solution circulation pump 4, the delivery port of the first solution water-supply-pipe 3 is connected with the water injector that is arranged on the wet exchange of return air heat recovery heat core body 5 internal upper parts,
Return air heat reclaims the wet exchange of heat core component and comprises that return air heat reclaims the wet exchange of heat core body 5, the bottom that return air heat reclaims the wet exchange of heat core body 5 has air inlet, the top that return air heat reclaims the wet exchange of heat core body 5 has air outlet, the below that return air heat reclaims the wet exchange of heat core body 5 is provided with the second solution tank 6, the bottom of the second solution tank 6 is connected with the water inlet of the second solution water-supply-pipe 7, the middle part of the second solution water-supply-pipe 7 is in series with the second solution circulation pump 8, the delivery port of the second solution water-supply-pipe 7 is connected with the water injector that is arranged on the wet exchange of new wind-heat recovery heat core body 1 internal upper part,
The air outlet that new wind-heat reclaims the wet exchange of heat core component is connected with the air inlet of Dehumidifying element heat exchange core body assembly by pipeline, Dehumidifying element heat exchange core body assembly comprises Dehumidifying element heat exchange core body 9, the bottom of Dehumidifying element heat exchange core body 9 has air inlet, the top of Dehumidifying element heat exchange core body 9 has air outlet, the below of Dehumidifying element heat exchange core body 9 is provided with the 3rd solution tank 10, the bottom of the 3rd solution tank 10 is connected with the water inlet of the 3rd solution water-supply-pipe 11, the middle part of the 3rd solution water-supply-pipe 11 is in series with the outer circulation path of the 3rd solution circulation pump 12 and vaporation-type plate type heat exchanger 13, the delivery port of the 3rd solution circulation pump 12 is connected with the water injector that is arranged on Dehumidifying element heat exchange core body 9 internal upper parts,
The air outlet that return air heat reclaims the wet exchange of heat core component is connected with the air inlet of regeneration unit heat exchange core body assembly by pipeline, regeneration unit heat exchange core body assembly comprises regeneration unit heat exchange core body 14, the bottom of regeneration unit heat exchange core body 14 has air inlet, the top of regeneration unit heat exchange core body 14 has air outlet, the below of regeneration unit heat exchange core body 14 is provided with the 4th solution tank 15, the bottom of the 4th solution tank 15 is connected with the water inlet of the 4th solution water-supply-pipe 16, the middle part of the 4th solution water-supply-pipe 16 is in series with the outer circulation path of the 4th solution circulation pump 17 and condensing plate type heat exchanger 18, the delivery port of the 4th solution circulation pump 17 is connected with the water injector that is arranged on regeneration unit heat exchange core body 14 internal upper parts,
The outlet of the refrigerant circulation path in vaporation-type plate type heat exchanger 13 is connected with the entrance of compressor 20 by pipeline, the outlet of compressor 20 is connected with the entrance of the refrigerant circulation path of condensing plate type heat exchanger 18 by pipeline, the outlet of the refrigerant circulation path of condensing plate type heat exchanger 18 is connected with the entrance of expansion valve 19 by pipeline, and the outlet of expansion valve 19 is connected with the entrance of the refrigerant circulation path of each vaporation-type plate type heat exchanger 13 by pipeline;
The delivery port of each the 3rd solution tank 10 bottom is connected with the water inlet of the left heat exchanger channels of plate type heat exchanger 23 by the 3rd solution flow pipe road 22 that is in series with the 3rd solution water-delivery pump 21 respectively, and the delivery port of the left heat exchanger channels of this plate type heat exchanger 23 is connected with the water inlet of the 4th solution tank 15;
The delivery port of each the 4th solution tank 15 bottom is connected with the water inlet of the right heat exchanger channels of plate type heat exchanger 23 by the 4th solution flow pipe road 25 that is in series with the 4th solution water-delivery pump 24 respectively, and the delivery port of the right heat exchanger channels of this plate type heat exchanger 23 is connected with the water inlet of the 3rd solution tank 10;
Each the 4th solution tank 15 is connected with the delivery port of filling pipe 26, is in series with pipe valve or water compensating valve 27 on filling pipe 26.The effect of filling pipe 26 is to the 4th solution tank 15 moisturizings, to control the concentration of solution.
The situation that the direction of arrow in the figure of the present embodiment is summer operation, in summer, salting liquid in the 3rd solution water-supply-pipe 11 that vaporation-type plate type heat exchanger 13 flows out for cooling the 3rd solution tank 10, to strengthen the dehumidifying effect of Dehumidifying element heat exchange core body 9, condensing plate type heat exchanger 18 heats the salting liquid in the 4th solution water-supply-pipe 16 flowed out in the 4th solution tank 15, to strengthen the power of regeneration of regeneration unit heat exchange core body 14.
The unit of present embodiment when operation air and the flow process of solution as follows:
At first new wind enter new wind-heat by the wet air inlet that exchanges core body 1 of new wind-heat recovery heat and reclaim in hot wet exchange core body 1, in new wind-heat, reclaim in the wet exchange of heat core body 1, new wind is higher by concentration, the preliminary precooling of the salting liquid that temperature is lower dehumidifies in advance, new wind after the pre-dehumidifying of precooling, air inlet by the wet exchange of Dehumidifying element heat core body 9 enters in Dehumidifying element heat exchange core body 9, in the wet exchange of Dehumidifying element heat core body 9, air is high by concentration, the further degree of depth dehumidifying of the salting liquid that temperature is low, after cooling, outlet by Dehumidifying element heat exchange core body 9 is flowed out, thereby send into indoor.
Return air for regeneration, at first reclaiming the wet entrance that exchanges core body 5 of heat by return air heat enters in the wet exchange of return air heat recovery heat core body, at return air heat, reclaim in the wet exchange of heat core body 5, return air is lower by concentration, the preliminary preheating of the salting liquid that temperature is higher and humidification, return air after the preheating pre-humidifying, entrance by regeneration unit heat exchange core body 14 enters in regeneration unit heat exchange core body 14, in the wet exchange of regeneration unit heat core body 14, air is high by concentration, the further degree of depth heating of the salting liquid that temperature is low, after humidification, outlet by regeneration unit heat exchange core body 14 is flowed out, and be discharged in outside atmosphere,
Reclaim the solution that temperature is higher, humidity is larger of the first solution tank 2 outflows of the wet exchange of heat core body 1 below from new wind-heat, through the first solution water-supply-pipe 3, the first solution circulation pump 4, the top inflow return air heat that reclaims the wet exchange of heat core body 5 from return air heat reclaims the wet exchange of heat core body 5, reclaim the wet exchange of heat core body 5 and flow down from return air heat again, and with flow into the return air that temperature is lower, humidity is lower that return air heat reclaims in the wet exchange of heat core body 5 and carry out the wet exchange of direct heat, then solution flows into the second solution tank 6;
By the solution after moisture and thermal release are in return air, its temperature reduces, concentration raises, the second solution tank 6 that the solution that temperature is lower, concentration is larger reclaims the wet exchange of heat core body 5 belows from return air heat flows out, the top of reclaiming the wet exchange of heat core body 1 from new wind-heat flows into, reclaim the wet exchange of heat core body 1 and flow down from new wind-heat again, finally flow into the first solution tank 2;
The higher salting liquid of concentration flowed out through circulation line from the 3rd solution tank 10 of the wet exchange of Dehumidifying element heat core body 9 belows, after vaporation-type plate type heat exchanger 13 is cooling, flow into the wet exchange of Dehumidifying element heat core body 9 from the top of the wet exchange of Dehumidifying element heat core body 9, from the wet heat exchange core body 9 of Dehumidifying element heat, flow down again, and carry out the wet exchange of direct heat with the air flowed in the wet exchange of Dehumidifying element heat core body 9, finally flow into the 3rd solution tank 10;
The concentration of salt solution that absorbs moisture in new wind reduces, by solution matter exchange cycles pipeline, enter in the 4th solution tank 15 of the wet exchange of regeneration unit heat core body 14 belows, and the lower salting liquid of concentration flowed out from the 4th solution tank 15, after 18 heating of condensing plate type heat exchanger, flow into the wet exchange of regeneration unit heat core body 14 from the top of the wet exchange of regeneration unit heat core body 14, from the wet exchange of regeneration unit heat core body 14, flow down again, and wet and exchange core body with inflow regeneration unit heat, air in 14 carries out the wet exchange of direct heat, then solution flows into the 4th solution tank 15, the concentration of salt solution that moisture is reproduced after new wind absorbs is higher, enters in the 3rd solution tank 10,
Carry out heat recovery by plate type heat exchanger 5 between weak solution from the 3rd solution tank 10 inflow the 4th solution tanks 15 and the concentrated solution flowed into the 3rd solution tanks 10 from the 4th solution tank 15.
Principle and the summer of unit winter operation are similar, difference is to make that refrigerant flow direction is contrary with summer condition moves, make summer as condensing plate type heat exchanger 18, transform into as the vaporation-type plate type heat exchanger, solution in the wet exchange of cooling regeneration unit heat core body 14 is cooling to the return air dehumidifying, and summer as vaporation-type plate type heat exchanger 13, as the solution in the wet exchange of condensing plate type heat exchanger warming and humidifying unit heat core body (be the wet exchange of Dehumidifying element heat core body summer), new wind is carried out to warming and humidifying; The new wind of the warm and moist after warming and humidifying is sent into indoor.
At transition season, unit is not opened compressor 20, only moves full heat recovery units, by solution, between the level of left and right, with the heat of air is wet, exchanges, and realizes full recuperation of heat operating mode operation, can realize to the new wind of indoor supply.
As shown in Figure 2, heat pump of the present utility model drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, can be also to comprise that new wind-heat reclaims heat wet exchange core component and return air heat reclaims the wet exchange of heat core component, wind-heat reclaims the wet exchange of heat core component and comprises that 2 new wind-heat reclaim the wet exchange of heat core body 1, the quantity that new wind-heat reclaims the wet exchange of heat core body 1 can be also 3 or 4 or 5 or 6 or more, the bottom that each new wind-heat reclaims the wet exchange of heat core body 1 has respectively air inlet, the top that each new wind-heat reclaims the wet exchange of heat core body 1 has respectively air outlet, the air outlet of the air inlet of the wet exchange of a new wind-heat recovery heat core body 1 and the wet exchange of another new wind-heat recovery heat core body 1 is mutually connected and is linked to be a hot wet interchange channel of new wind-heat recovery by airduct, the below that each new wind-heat reclaims the wet exchange of heat core body 1 is respectively equipped with the first solution tank 2, the bottom of each the first solution tank 2 is connected with the water inlet of the first solution water-supply-pipe 3 respectively, the middle part of each the first solution water-supply-pipe 3 is in series with respectively the first solution circulation pump 4, the delivery port of each the first solution water-supply-pipe 3 is connected with the water injector that is arranged on the wet exchange of return air heat recovery heat core body 5 internal upper parts,
Return air heat reclaims the wet exchange of heat core component and comprises that 2 return air heats reclaim the wet exchange of heat core body 5, the quantity that return air heat reclaims the wet exchange of heat core body 5 can be also 3 or 4 or 5 or 6 or more, the bottom that each return air heat reclaims the wet exchange of heat core body 5 has respectively air inlet, the top that each return air heat reclaims the wet exchange of heat core body 5 has respectively air outlet, the air outlet of the air inlet of the wet exchange of a return air heat recovery heat core body 5 and the wet exchange of another return air heat recovery heat core body 5 is mutually connected and is linked to be a hot wet interchange channel of return air heat recovery by airduct, the below that each return air heat reclaims the wet exchange of heat core body 5 is respectively equipped with the second solution tank 6, the bottom of each the second solution tank 6 is connected with the water inlet of the second solution water-supply-pipe 7 respectively, the middle part of each the second solution water-supply-pipe 7 is in series with respectively the second solution circulation pump 8, the delivery port of each the second solution water-supply-pipe 7 is connected with the water injector that is arranged on the wet exchange of new wind-heat recovery heat core body 1 internal upper part,
The air outlet that new wind-heat reclaims the wet exchange of heat core component is connected with the air inlet of Dehumidifying element heat exchange core body assembly by pipeline, Dehumidifying element heat exchange core body assembly comprises 2 Dehumidifying element heat exchange core bodies 9, the quantity of Dehumidifying element heat exchange core body 9 can be also 3 or 4 or 5 or 6 or more, the bottom of each Dehumidifying element heat exchange core body 9 has respectively air inlet, the top of each Dehumidifying element heat exchange core body 9 has respectively air outlet, the air outlet of the air inlet of a Dehumidifying element heat exchange core body 9 and another Dehumidifying element heat exchange core body 9 is mutually connected and is linked to be a dehumidifying heat exchanger channels by airduct, the below of each Dehumidifying element heat exchange core body 9 is respectively equipped with the 3rd solution tank 10, the bottom of each the 3rd solution tank 10 is connected with the water inlet of the 3rd solution water-supply-pipe 11 respectively, the middle part of each the 3rd solution water-supply-pipe 11 is in series with respectively the outer circulation path of the 3rd solution circulation pump 12 and vaporation-type plate type heat exchanger 13, the delivery port of each the 3rd solution circulation pump 12 is connected with the water injector that is arranged on Dehumidifying element heat exchange core body 9 internal upper parts,
The air outlet that return air heat reclaims the wet exchange of heat core component is connected with the air inlet of regeneration unit heat exchange core body assembly by pipeline, regeneration unit heat exchange core body assembly comprises 2 regeneration unit heat exchange core bodies 14, the quantity of regeneration unit heat exchange core body 14 can be also 3 or 4 or 5 or 6 or more, the bottom of each regeneration unit heat exchange core body 14 has respectively air inlet, the top of each regeneration unit heat exchange core body 14 has respectively air outlet, the air outlet of the air inlet of a regeneration unit heat exchange core body 14 and another regeneration unit heat exchange core body 14 is mutually connected and is linked to be a regeneration passage by airduct, the below of each regeneration unit heat exchange core body 14 is respectively equipped with the 4th solution tank 15, the bottom of each the 4th solution tank 15 is connected with the water inlet of the 4th solution water-supply-pipe 16 respectively, the middle part of each the 4th solution water-supply-pipe 16 is in series with respectively the outer circulation path of the 4th solution circulation pump 17 and condensing plate type heat exchanger 18, the delivery port of each the 4th solution circulation pump 17 is connected with the water injector that is arranged on regeneration unit heat exchange core body 14 internal upper parts,
The outlet of the refrigerant circulation path in each vaporation-type plate type heat exchanger 13 is connected with the entrance of compressor 20 by pipeline, the outlet of compressor 20 is connected with the entrance of the refrigerant circulation path of each condensing plate type heat exchanger 18 by pipeline, the outlet of the refrigerant circulation path of each condensing plate type heat exchanger 18 is connected with the entrance of expansion valve 19 by pipeline, and the outlet of expansion valve 19 is connected with the entrance of the refrigerant circulation path of each condensing plate type heat exchanger 18 by pipeline;
The delivery port of each the 3rd solution tank 10 bottom is connected with the water inlet of the left heat exchanger channels of plate type heat exchanger 23 by the 3rd solution flow pipe road 22 that is in series with the 3rd solution water-delivery pump 21 respectively, and the delivery port of the left heat exchanger channels of this plate type heat exchanger 23 is connected with the water inlet of the 4th solution tank 15;
The delivery port of each the 4th solution tank 15 bottom is connected with the water inlet of the right heat exchanger channels of plate type heat exchanger 23 by the 4th solution flow pipe road 25 that is in series with the 4th solution water-delivery pump 24 respectively, and the delivery port of the right heat exchanger channels of this plate type heat exchanger 23 is connected with the water inlet of the 3rd solution tank 10;
Each the 4th solution tank 15 is connected with the delivery port of filling pipe 26, is in series with pipe valve or water compensating valve 27 on filling pipe 26.
In above-described embodiment, the quantity of compressor 20 and expansion valve 19 is 2, and the quantity of compressor 20 and expansion valve 19 also can be 3 or 4 or 5 or 6.
Embodiment difference shown in present embodiment and Fig. 1 is, present embodiment is the wet exchange of a plurality of new wind-heat recovery heat core body 1 of having connected, a plurality of return air heats reclaim the wet exchange of heat core body 5, a plurality of Dehumidifying element heat exchange core bodies 9 and a plurality of regeneration unit heat exchange core body 14, the operation principle of present embodiment is basic identical with the operation principle of the embodiment shown in Fig. 1, its difference only allows needs air-flow to be processed to pass the wet exchange of a plurality of new wind-heat recovery heat core body 1, a plurality of return air heats reclaim the wet exchange of heat core body 5, a plurality of Dehumidifying element heat exchange core bodies 9 and a plurality of regeneration unit heat exchange core body 14.
Heat pump shown in Fig. 3 drives the solution humidifying air-conditioning system of the wet exchange of refluent heat and the heat pump shown in Fig. 2 to drive the solution humidifying air-conditioning system of the wet exchange of refluent heat basic identical, difference is: each the group vaporation-type plate type heat exchanger 13 in the solution humidifying air-conditioning system of the wet exchange of heat pump driving refluent heat shown in Fig. 3 and condensing plate type heat exchanger 18 be a corresponding compressor 20 and an expansion valve 19 all, i.e. the hot wet exchange core body of the dehumidifying of every one-level and regeneration unit is used independently refrigeration system.Physical device adopts any pattern, depends on the capacity of concrete air dewetting, amount of cooling water and refrigeration system.By regulating the cold of each vaporation-type plate type heat exchanger of refrigeration system, can regulate the temperature of dehumidification solutions at different levels, control the concentration of dehumidification solutions at different levels by suitable moisturizing simultaneously, progressively dehumidifying and the cooling of realization to new wind, to reduce the irreversible loss of process, improve the Energy Efficiency Ratio (OP) that unit is processed new wind.
The utility model only describes with above-mentioned three kinds of the most common embodiments; the other forms of unit obtained under enlightenment of the present utility model; every conversion of indivedual parts being carried out according to basic principle of the present utility model or improvement, all within its protection domain.
Claims (2)
1. heat pump drives the solution humidifying air-conditioning system of the wet exchange of refluent heat, it is characterized in that: comprise that new wind-heat reclaims heat wet exchange core component and return air heat reclaims the wet exchange of heat core component, wind-heat reclaims the wet exchange of heat core component and comprises that more than one new wind-heat reclaims the wet exchange of heat core body (1), the bottom that each new wind-heat reclaims heat wet exchange core body (1) has respectively air inlet, the top that each new wind-heat reclaims heat wet exchange core body (1) has respectively air outlet, the air outlet of the air inlet of a new wind-heat recovery heat wet exchange core body (1) and another new wind-heat recovery heat wet exchange core body (1) is mutually connected and is linked to be a hot wet interchange channel of new wind-heat recovery by airduct, the below that each new wind-heat reclaims heat wet exchange core body (1) is respectively equipped with the first solution tank (2), the bottom of each the first solution tank (2) is connected with the water inlet of the first solution water-supply-pipe (3) respectively, the middle part of each the first solution water-supply-pipe (3) is in series with respectively the first solution circulation pump (4), the delivery port of each the first solution water-supply-pipe (3) is connected with the water injector that is arranged on the wet exchange of return air heat recovery heat core body (5) internal upper part,
Described return air heat reclaims the wet exchange of heat core component and comprises that more than one return air heat reclaims the wet exchange of heat core body (5), the bottom that each return air heat reclaims heat wet exchange core body (5) has respectively air inlet, the top that each return air heat reclaims heat wet exchange core body (5) has respectively air outlet, the air outlet of the air inlet of a return air heat recovery heat wet exchange core body (5) and another return air heat recovery heat wet exchange core body (5) is mutually connected and is linked to be a hot wet interchange channel of return air heat recovery by airduct, the below that each return air heat reclaims heat wet exchange core body (5) is respectively equipped with the second solution tank (6), the bottom of each the second solution tank (6) is connected with the water inlet of the second solution water-supply-pipe (7) respectively, the middle part of each the second solution water-supply-pipe (7) is in series with respectively the second solution circulation pump (8), the delivery port of each the second solution water-supply-pipe (7) is connected with the water injector that is arranged on the wet exchange of new wind-heat recovery heat core body (1) internal upper part,
The air outlet that described new wind-heat reclaims the wet exchange of heat core component is connected with the air inlet of Dehumidifying element heat exchange core body assembly by pipeline, Dehumidifying element heat exchange core body assembly comprises more than one Dehumidifying element heat exchange core body (9), the bottom of each Dehumidifying element heat exchange core body (9) has respectively air inlet, the top of each Dehumidifying element heat exchange core body (9) has respectively air outlet, the air outlet of the air inlet of a Dehumidifying element heat exchange core body (9) and another Dehumidifying element heat exchange core body (9) is mutually connected and is linked to be a dehumidifying heat exchanger channels by airduct, the below of each Dehumidifying element heat exchange core body (9) is respectively equipped with the 3rd solution tank (10), the bottom of each the 3rd solution tank (10) is connected with the water inlet of the 3rd solution water-supply-pipe (11) respectively, the middle part of each the 3rd solution water-supply-pipe (11) is in series with respectively the outer circulation path of the 3rd solution circulation pump (12) and vaporation-type plate type heat exchanger (13), the delivery port of each the 3rd solution circulation pump (12) is connected with the water injector that is arranged on Dehumidifying element heat exchange core body (9) internal upper part,
The air outlet that described return air heat reclaims the wet exchange of heat core component is connected with the air inlet of regeneration unit heat exchange core body assembly by pipeline, regeneration unit heat exchange core body assembly comprises more than one regeneration unit heat exchange core body (14), the bottom of each regeneration unit heat exchange core body (14) has respectively air inlet, the top of each regeneration unit heat exchange core body (14) has respectively air outlet, the air outlet of the air inlet of a regeneration unit heat exchange core body (14) and another regeneration unit heat exchange core body (14) is mutually connected and is linked to be a regeneration passage by airduct, the below of each regeneration unit heat exchange core body (14) is respectively equipped with the 4th solution tank (15), the bottom of each the 4th solution tank (15) is connected with the water inlet of the 4th solution water-supply-pipe (16) respectively, the middle part of each the 4th solution water-supply-pipe (16) is in series with respectively the outer circulation path of the 4th solution circulation pump (17) and condensing plate type heat exchanger (18), the delivery port of each the 4th solution circulation pump (17) is connected with the water injector that is arranged on regeneration unit heat exchange core body (14) internal upper part,
The outlet of the refrigerant circulation path in each described vaporation-type plate type heat exchanger (13) is connected with the entrance of compressor (20) by pipeline, the outlet of compressor (20) is connected by the entrance of the refrigerant circulation path of the described condensing plate type heat exchanger of pipeline and each (18), the outlet of the refrigerant circulation path of each described condensing plate type heat exchanger (18) is connected with the entrance of expansion valve (19) by pipeline, and the outlet of expansion valve (19) is connected by the entrance of the refrigerant circulation path of the described vaporation-type plate type heat exchanger of pipeline and each (13);
The delivery port of each described the 3rd solution tank (10) bottom is connected with the water inlet of the left heat exchanger channels of plate type heat exchanger (23) by the 3rd solution flow pipe road (22) that is in series with the 3rd solution water-delivery pump (21) respectively, and the delivery port of the left heat exchanger channels of this plate type heat exchanger (23) is connected with the water inlet of described the 4th solution tank (15);
The delivery port of each described the 4th solution tank (15) bottom is connected with the water inlet of the right heat exchanger channels of described plate type heat exchanger (23) by the 4th solution flow pipe road (25) that is in series with the 4th solution water-delivery pump (24) respectively, and the delivery port of the right heat exchanger channels of this plate type heat exchanger (23) is connected with the water inlet of described the 3rd solution tank (10);
Each described the 4th solution tank (15) is connected with the delivery port of filling pipe (26), is in series with pipe valve or water compensating valve (27) on filling pipe (26).
2. drive the solution humidifying air-conditioning system of the wet exchange of refluent heat according to heat pump claimed in claim 1, it is characterized in that: described new wind-heat reclaims the wet exchange of heat core body (1), described return air heat reclaims the wet exchange of heat core body (5), described Dehumidifying element heat exchange core body (9), described regeneration unit heat exchange core body (14), described the first solution tank (2), described the second solution tank (6), described the 3rd solution tank (10), the quantity of described the 4th solution tank (15) is all 2 or 3 or 4 or 5 or 6, the quantity of described compressor (20) and described expansion valve (19) is 2 or 3 or 4 or 5 or 6.
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| CN 201220565530 CN202955793U (en) | 2012-09-29 | 2012-10-31 | Heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system |
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| CN201220503621.8 | 2012-09-29 | ||
| CN201220503621 | 2012-09-29 | ||
| CN 201220565530 CN202955793U (en) | 2012-09-29 | 2012-10-31 | Heat pump drive reverse flow heat-humidity exchange solution humidifying air conditioner system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103090475A (en) * | 2012-09-29 | 2013-05-08 | 刘拴强 | Heat pump-driven countercurrent heat and moisture exchange liquid desiccant air conditioning system |
| CN109186015A (en) * | 2018-08-13 | 2019-01-11 | 珠海格力电器股份有限公司 | The control method of air-conditioning system and air-conditioning system |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106369706B (en) * | 2016-10-31 | 2018-02-02 | 天津商业大学 | A kind of salting liquid heat pump regeneration system based under vacuum |
| CN113983572B (en) * | 2021-10-26 | 2023-05-12 | 上海建工集团股份有限公司 | Control system and method for solution heat recovery device |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4941324A (en) * | 1989-09-12 | 1990-07-17 | Peterson John L | Hybrid vapor-compression/liquid desiccant air conditioner |
| CN1217143C (en) * | 2003-09-26 | 2005-08-31 | 清华大学 | Solution full heat recovery type fresh air conditioner |
| CN100451468C (en) * | 2006-06-15 | 2009-01-14 | 清华大学 | Multi-stage solution dehumidifying and regenerating fresh air set driven by heat pump |
| CN101706136B (en) * | 2009-11-21 | 2012-04-18 | 青岛大学 | Solution temperature and humidity adjustment air treatment system |
| CN201582927U (en) * | 2009-11-26 | 2010-09-15 | 佛山市浩特普尔人工环境设备有限公司 | Coupling counterflow-type solution dehumidification fresh air system of heat pump |
| CN102563786B (en) * | 2012-01-12 | 2014-04-23 | 西安交通大学 | Refrigeration and heat pump composite energy system with independently controlled temperature and independently controlled humidity |
| CN103090475B (en) * | 2012-09-29 | 2015-06-10 | 刘拴强 | Heat pump-driven countercurrent heat and moisture exchange liquid desiccant air conditioning system |
-
2012
- 2012-10-31 CN CN201210425772.0A patent/CN103090475B/en active Active
- 2012-10-31 CN CN 201220565530 patent/CN202955793U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103090475A (en) * | 2012-09-29 | 2013-05-08 | 刘拴强 | Heat pump-driven countercurrent heat and moisture exchange liquid desiccant air conditioning system |
| CN103090475B (en) * | 2012-09-29 | 2015-06-10 | 刘拴强 | Heat pump-driven countercurrent heat and moisture exchange liquid desiccant air conditioning system |
| CN109186015A (en) * | 2018-08-13 | 2019-01-11 | 珠海格力电器股份有限公司 | The control method of air-conditioning system and air-conditioning system |
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| CN103090475A (en) | 2013-05-08 |
| CN103090475B (en) | 2015-06-10 |
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Assignee: BEIJING GERUI LIDE AIR CONDITIONER TECHNOLOGY CO., LTD. Assignor: Liu Shuanqiang Contract record no.: 2013990000518 Denomination of utility model: Heat pump-driven countercurrent heat and moisture exchange liquid desiccant air conditioning system Granted publication date: 20130529 License type: Exclusive License Record date: 20130827 |
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Assignee: BEIJING GERUI LIDE AIR CONDITIONER TECHNOLOGY CO., LTD. Assignor: Liu Shuanqiang Contract record no.: 2013990000518 Date of cancellation: 20151030 |
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