CN204513624U - A kind of heat pump driven dehumidification solution temperature controls and domestic hot-water's device for making - Google Patents
A kind of heat pump driven dehumidification solution temperature controls and domestic hot-water's device for making Download PDFInfo
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- CN204513624U CN204513624U CN201420799869.2U CN201420799869U CN204513624U CN 204513624 U CN204513624 U CN 204513624U CN 201420799869 U CN201420799869 U CN 201420799869U CN 204513624 U CN204513624 U CN 204513624U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 238000007791 dehumidification Methods 0.000 title claims abstract description 33
- 239000002904 solvent Substances 0.000 claims abstract description 25
- 239000000498 cooling water Substances 0.000 claims abstract description 21
- 230000008676 import Effects 0.000 claims description 11
- 239000002826 coolant Substances 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 6
- 239000003507 refrigerant Substances 0.000 claims description 4
- 239000008399 tap water Substances 0.000 claims 2
- 235000020679 tap water Nutrition 0.000 claims 2
- 238000009833 condensation Methods 0.000 abstract description 13
- 230000005494 condensation Effects 0.000 abstract description 13
- 238000002360 preparation method Methods 0.000 abstract 1
- 230000008929 regeneration Effects 0.000 description 14
- 238000011069 regeneration method Methods 0.000 description 14
- 238000000034 method Methods 0.000 description 11
- 230000008569 process Effects 0.000 description 9
- 238000001816 cooling Methods 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000002918 waste heat Substances 0.000 description 6
- 238000010792 warming Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 230000001932 seasonal effect Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000006200 vaporizer Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
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Abstract
The utility model discloses a kind of heat pump driven dehumidification solution temperature to control and domestic hot-water's device for making.It is characterized in that: described device comprises heat pump assembly, solution humidifying device; Described heat pump assembly comprises frequency-changeable compressor, four-way change-over valve, solution cooler condenser, check-valves, choke valve and evaporimeter, is also provided with water-cooled condenser and carries out producing of domestic hot-water; Described solution humidifying device contains dehumidifier, regenerator, solution pump, solution heat exchanger, solvent valve and blower fan; Solution recycle system, heat pump and domestic water preparation system combine by the utility model, dehumidification solution amount of cooling water and the demand adding heat in solution humidifying system is met under heat pump drives, utilize unnecessary condensation heat to produce domestic water simultaneously, reach effective utilization of the energy, there is good market prospects and value.
Description
Technical field
The utility model relates to a kind of heat pump driven dehumidification solution temperature and controls and domestic hot-water's device for making, and belong to solution dehumidification technology category, the condensation heat of heat pump produces domestic hot-water field.
Background technology
Adopt solution dehumidification technology that low-grade heat source can be utilized to realize the wet independent process of air heat, it gains public acceptance in the advantage in energy-conservation.In addition its good environmental acceptability, help advantages such as improving indoor air quality, solution dehumidification system and the air-conditioning system based on solution dehumidification technology obtain in recent years to be paid close attention to widely.
When the waste heat not having directly available, temperature grade to be suitable for is to meet regeneration of waste liquor demand, heat pump driven solution humidifying air processor can be adopted.In such solution humidifying air processor, be provided with heat pump cycle in unit, the heat exhaust of heat pump condenser is used for concentrating regenerative solution, and the cold of evaporator with heat pump is used for cooling and dehumidifying solution, improves its dehumidifying effect.If solution humidifying mode effectively can be combined with heat pump cycle, respective advantage can be given full play to, contribute to the Effec-tive Function realizing air humidity processing procedure.
Along with improving constantly of people's living standard, require also to promote to the comfortableness of living environment, to the demand of domestic hot-water also in continuous rising thereupon.Correlative study shows, when the cold that the evaporimeter in heat pump provides reaches service requirement, the heat exhaust of condenser is often too much, causes the imbalance of system capacity.In order to make the condensation heat of this part be fully used, heat pump can set up domestic hot-water's device for making, utilizes system heat more than needed to produce domestic hot-water, takes full advantage of the energy, decrease the energy resource consumption of producing domestic hot-water specially, energy-conserving and environment-protective.
Summary of the invention
Goal of the invention: in order to solve the energy balance problem in heat pump and solution humidifying set composite, the utility model provides a kind of heat pump driven dehumidification solution temperature to control and domestic hot-water's device for making.
Technical scheme: the heat pump driven dehumidification solution temperature that the utility model proposes controls and domestic hot-water's device for making, it is characterized in that: described device comprises heat pump assembly and solution humidifying device, described heat pump assembly comprises: frequency-changeable compressor 3, the four-way change-over valve 18 be connected by pipeline with frequency-changeable compressor 3, the solution cooler condenser 5 be connected by pipeline with four-way change-over valve 18, with solution cooler condenser 5 by pipeline and check-valves 17a, choke valve 4b, the water-cooled condenser 7 that check-valves 17b is connected, with water-cooled condenser 7 by pipeline and choke valve 4a, check-valves 17c, the evaporimeter 6 that check-valves 17d is connected, described evaporimeter 6 is connected by pipeline with four-way change-over valve 18, described solution humidifying device comprises: dehumidifier 1, the solution heat exchanger 10 be connected by pipeline and solvent valve with dehumidifier 1, the solution pump 8 be connected by pipeline with solution heat exchanger 10, the regenerator 2 be connected by pipeline with solution pump 8, the solution pump 9 that is connected by pipeline with solution heat exchanger 10, described regenerator 2 is connected by pipeline and solvent valve with solution heat exchanger 10, and described solution pump 9 is connected by pipeline with dehumidifier 1.
Further, arrange water-cooled condenser 7 in heat pump between solution cooler condenser 5 and evaporimeter 6, centre is connected by refrigerant tubing and valve, forms chilled water unit to produce domestic hot-water.
Chilled water unit is by water-cooled condenser access heat pump assembly, the import of water-cooled condenser 7 is connected with solution cooler condenser 5 by pipeline, the outlet of water-cooled condenser 7 is connected with choke valve 4a or choke valve 4b by pipeline, and choke valve is connected with evaporimeter 6 by pipeline.Described water-cooled condenser 7 is respectively equipped with cooling water inlet 7a and coolant outlet 7b, the pipeline between cooling water inlet 7a and water-cooled condenser 7 is arranged water regulating valve 19 for regulating pondage.Like this can on the basis meeting regeneration of waste liquor heat demand, the unnecessary condensation heat making full use of heat pump assembly produces domestic hot-water, realizes system capacity balance, economize energy.
Evaporimeter 6 in described heat pump assembly is connected with the dehumidifier 1 of solution humidifying device by pipeline, and the solution cooler condenser 5 in heat pump assembly is connected with the regenerator 2 of solution humidifying device by pipeline.
In described solution humidifying device, the low temperature weak solution that dehumidifier 1 exports and the high temperature concentrated solution that regenerator 2 exports enter in solution heat exchanger 10 respectively carries out exchange heat.
The concentrated solution of described solution heat exchanger 10 import and weak solution pipeline arrange solvent valve 11 and solvent valve 12 respectively.The outlet of dehumidifier 1 arranges solvent valve 14, and the outlet of regenerator 2 arranges solvent valve 13.
Described dehumidifier 1 and regenerator 2 arrange blower fan 15 and blower fan 16 respectively, the air blower import 1c on corresponding dehumidifier and air outlet slit 1d, the air intlet 2c on regenerator 2 and air outlet slit 2d.
This device is applicable to summer and winter condition simultaneously, and check-valves 17a is connected with choke valve 4b by pipeline, and check-valves 17a is in parallel with check-valves 17b, and circulating direction is contrary; Check-valves 17c is connected with choke valve 4a by pipeline, and check-valves 17c is in parallel with check-valves 17d, and circulating direction is contrary.By the switching of four-way change-over valve 18, that be in circulation status under summer condition is check-valves 17b, check-valves 17c and choke valve 4a, that be in circulation status under winter condition is check-valves 17a, check-valves 17d and choke valve 4b, dehumidifier 1 carries out cool-down dehumidification in summer to new wind, carries out warming and humidifying in the winter time to new wind.
Heat pump assembly combines with solution humidifying device by the utility model, in solution circulation process there is the demand being heated and be cooled in the dehumidifying of solution and regenerative process, in heat pump driven solution humidifying device, the condensation heat in heat pump cycle can be used for thermal regeneration solution; Vaporizer side simultaneously in heat pump cycle can also provide cold, reduces the temperature that solution enters dehumidifier, contributes to the temperature rise suppressing dehumidification process, makes the dehumidifying effect that solution keeps stronger.Solution humidifying mode and heat pump cycle are effectively combined, respective advantage can be given full play to, contribute to the Effec-tive Function realizing air humidity processing procedure.In addition, because whole system exists the imbalance of energy, the condensation heat that heat pump can provide is still too much, in order to this part waste heat is fully utilized, a water-cooled condenser is set between the condensator outlet end, choke valve entrance point of heat pump assembly, produces a part of domestic hot-water with this part waste heat.Can, according to the solution chilling temperature of setting, regulate the frequency of frequency-changeable compressor to reach the requirement of cooling solution institute chilling requirement in system.Simultaneously, according to the regeneration of waste liquor temperature regulating pondage control valve of setting, with adjusting heat pump condensation heat in solution and cooling water allocation proportion between the two, meet the requirement of regeneration of waste liquor institute calorific requirement in system, thus finally realize system energy balance between cold and heat is provided.For summer, on water-cooled condenser, cooling water inlet water temperature is about 20 DEG C, the high pressure refrigerant liquid generation exchange heat that cooling water is discharged in water-cooled condenser and from solution condenser, absorb gasification latent heat and sensible heat, coolant outlet water temperature reaches about 35 ~ 40 DEG C, domestic hot-water's demand of general user can be met, take full advantage of the condensation heat of heat pump, save the energy.In like manner, winter, heat pump assembly was through the conversion of four-way change-over valve, system waste heat can be utilized equally to produce a part of domestic hot-water, now in water-cooled condenser, the inlet temperature of cooling water is about 10 DEG C, in water-cooled condenser and after cold-producing medium generation exchange heat, the water temperature of coolant outlet can reach about 30 DEG C, can meet general user's domestic hot-water's demand in the winter time equally, or reduces the heating energy consumption of domestic hot-water.
The cooling water entering water-cooled condenser in the utility model is the running water of this season normal temperature, easily absorbs and does not have the restriction in temperature, handled easily.
The heat pump driven solution humidifying device that the utility model relates to can carry out heat and wet treatment to indoor required new wind, and summer, winter realized warming and humidifying to its cool-down dehumidification, meets personnel and to wet demand in the heat that Various Seasonal is different to indoor environment.
Beneficial effect:
1. the waste heat produced in heat pump assembly is fully utilized and produce a part of domestic hot-water, saved the energy, reduce the energy consumption produced separately domestic hot-water and produce.
2. heat pump driven solution humidifying set composite is less than single solution humidifying plant energy consumption, when not having the suitable waste heat of temperature grade directly to utilize, the condensation heat of heat pump can meet regeneration of waste liquor needs, the evaporation side cold of heat pump, then for cooling and dehumidifying solution, can improve dehumidifying effect and suppress dehumidification process temperature rise.
3. the heat pump driven solution humidifying device that relates to of the utility model can carry out heat and wet treatment to indoor required new wind, and summer, winter realized warming and humidifying to its cool-down dehumidification, meets personnel and to wet demand in the heat that Various Seasonal is different to indoor environment.
4. the cooling water entering water-cooled condenser in the utility model is the running water of this season normal temperature, easily absorbs and does not have the restriction in temperature, handled easily.
5. by the condensation heat of efficiency utilization heat pump assembly, thus the energy balance problem existed in heat pump and solution humidifying set composite can be solved, the normal operation of assurance device.
Accompanying drawing explanation
Fig. 1 is that the heat pump driven dehumidification solution temperature that the utility model proposes controls and domestic hot-water's device for making schematic diagram.
Have in figure: dehumidifier 1, regenerator 2, frequency-changeable compressor 3, choke valve 4a, choke valve 4b (winter), solution condenser 5, evaporimeter 6, water-cooled condenser 7, solution pump 8, solution pump 9, solution heat exchanger 10, solvent valve 11, solvent valve 12, solvent valve 13, solvent valve 14, blower fan 15, blower fan 16, check-valves 17a (winter), check-valves 17b, check-valves 17c, check-valves 17d (winter), four-way change-over valve 18; Dehumidifier concentrated solution input 1a, dehumidifier weak solution output 1b, dehumidifier air blower import 1c, dehumidifier air outlet slit 1d, regenerator weak solution input 2a, regenerator concentrated solution output 2b, regenerator air fan inlet 2c, regenerator air outlet 2d, water-cooled condenser cooling water inlet 7a, water-cooled condenser coolant outlet 7b, water regulating valve 19.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further described.
Represent refrigerant flow circuit referring to solid line in Fig. 1, figure, dotted line represents solution flow process, and chain line represents Water flow-path.Whole device is made up of a heat pump cycle (comprising chilled water unit) and a solution circulation.
The four-way change-over valve 18 that described heat pump cycle comprises frequency-changeable compressor 3, be connected by pipeline with frequency-changeable compressor 3, the solution cooler condenser 5 be connected by pipeline with four-way change-over valve 18, the water-cooled condenser 7 be connected by pipeline and check-valves 17a, choke valve 4b, check-valves 17b with solution cooler condenser 5, the evaporimeter 6 that is connected by pipeline and choke valve 4a, check-valves 17c, check-valves 17d with water-cooled condenser 7, described evaporimeter 6 is connected by pipeline with four-way change-over valve 18; The solution heat exchanger 10 that described solution circulation comprises dehumidifier 1, be connected by pipeline and solvent valve with dehumidifier 1, the solution pump 8 be connected by pipeline with solution heat exchanger 10, the regenerator 2 be connected by pipeline with solution pump 8, the solution pump 9 that is connected by pipeline with solution heat exchanger 10, described regenerator 2 is connected by pipeline and solvent valve with solution heat exchanger 10, and described solution pump 9 is connected by pipeline with dehumidifier 1.The cold that the vaporizer side of heat pump cycle provides is for cooling solution, and to strengthen its dehumidifying effect and to suppress dehumidification process temperature rise, the heat extraction of condenser is used for thermal regeneration solution.Meanwhile, the after-heat produced due to system capacity imbalance is used for adding hot cooling water, provides a part of domestic hot-water.New wind needed for indoor air-conditioning system is by the process of solution humidifying device, and in cooled dehumidifying in summer, winter is by warming and humidifying.
In operation, according to the solution chilling temperature of setting, regulate the frequency of frequency-changeable compressor 3 to reach the requirement of cooling solution institute chilling requirement in system.Simultaneously, according to the regeneration of waste liquor temperature regulating pondage control valve 19 of setting, with adjusting heat pump condensation heat in solution and cooling water allocation proportion between the two, meet the requirement of regeneration of waste liquor institute calorific requirement in system, thus finally realize system energy balance between cold and heat is provided.
As shown in Figure 1, during summer condition: in dehumidifier 1, processed air is entered by the fan inlet 1c of dehumidifier 1, is discharged after dehumidified by the air outlet slit 1d of dehumidifier 1; Dehumidifying concentrated solution evenly sprays at filling surface through the nozzle of dehumidifier 1 import 1a, difference due to the partial pressure of water vapor on the partial pressure of water vapor in dehumidified air and dehumidification solution surface creates the motive force of dehumidification process, with moisture in air by solution absorb the heat of condensation of releasing solution temperature can be caused to raise, solution surface partial pressure of water vapor is corresponding rising also, the concentration of dehumidification solution reduces gradually, and weak solution flows out from dehumidifier outlet 1b; Weak solution enters solution heat exchanger 10 after flowing through solvent valve 14 and solvent valve 12 by pipeline, exchange heat is carried out with the high temperature concentrated solution flowed out from regenerator 2, temperature flows through solution pump 8 after raising, enter solution cooler condenser 5, solution condensation heat extraction in this sorption type heat pump system, after temperature is heated to the regeneration temperature of setting, regenerator is entered by import 2a, in regenerator 2, moisture is discharged to the regeneration air entered by fan inlet 2c by solution, regeneration air is discharged from air outlet slit 2d, and the solution now flowed out from taphole 2b is concentrated.Between solution cooler condenser 5 and evaporimeter 6, water-cooled condenser 7, choke valve 4a, choke valve 4b, check-valves 17a, check-valves 17b, check-valves 17c and check-valves 17d has been accessed respectively in heat pump assembly.When device is operated in summer condition, check-valves 17b and check-valves 17c is in circulation status, cold-producing medium exports successively through check-valves 17b, water-cooled condenser 7, choke valve 4a, check-valves 17c from solution cooler condenser 5, flow into evaporimeter 6, in evaporimeter, solution is cooled to the dehumidifier inlet temperature of setting, its dehumidifying effect is enhanced, and inhibits the solution temperature rise of dehumidification process.The cooling water flowed into from cooling water inlet 7a carries out exchange heat with the cold-producing medium flowed out from solution condensator outlet, after cooling water absorption refrigeration agent liberated heat, temperature raises, flow out from coolant outlet 7b, this part domestic hot-water meets a part of demand of user, has saved the energy.
During winter condition: the mutual conversion being realized evaporimeter 6 and solution cooler condenser 5 function by the switching of four-way change-over valve 18, but the function of water-cooled condenser 7 remains unchanged, and meanwhile, the effect of regenerator 2 and dehumidifier 1 is also exchanged.Dehumidifier 1 function in the winter time regenerates solution, regeneration air is the new wind that outdoor temperature is lower, thus humidification function can be realized to new wind, regenerator 2 function in the winter time becomes dehumidifying, absorb the moisture in indoor exhaust wind, solution concentration is reduced, provides condition for heating subsequently through heat pump assembly and then carry out humidification to new wind.Specific as follows: the return air that indoor humidity is higher is entered by the fan inlet 2c of regenerator 2 (winter is converted to dehumidification function), concentrated solution evenly sprays at filling surface through the nozzle of regenerator 2 import 2a, exported by 2d after moisture in indoor return air is absorbed by concentrated solution and discharge, solution heat exchanger 10 is entered after the weak solution that 2b outlet is discharged flows through solvent valve 13 and solvent valve 11, exchange heat is carried out with the high temperature concentrated solution flowed out from dehumidifier 1, temperature flows through solution pump 9 after reducing, enter evaporimeter 6 (winter is solution condenser modes), solution absorption refrigeration agent liberated heat, be heated to the regeneration temperature of setting, dehumidifier 1 (winter is converted to humidification function) is entered through import 1a, hot and humid area is carried out with the new wind in outdoor entered through fan inlet 1c, moisture is discharged to new wind, exported by 1d after making new wind be able to warming and humidifying and send into indoor.Solution heat exchanger 10 is entered after the concentrated solution that 1b outlet is flowed out flows through solvent valve 14 and solvent valve 12 successively, exchange heat is carried out with the low temperature weak solution flowed out from regenerator 2 (winter is converted to dehumidification function), temperature flows through solution pump 8 after reducing, enter solution cooler condenser 5 (winter is converted to solution evaporator mode), solution this cooled dose cooling, temperature be lowered to setting except again entering regenerator 2 through import 2a after wet temp.When device is operated in that winter, new wind added under wet cooling condition, check-valves 17a and check-valves 17d is in circulation status, cold-producing medium exports successively through check-valves 17d, water-cooled condenser 7, choke valve 4b, check-valves 17a from evaporimeter 6, flows into solution cooler condenser 5 (winter is evaporator mode).The cooling water flowed into from cooling water inlet 7a with export from evaporimeter 6 (winter is solution condenser modes) cold-producing medium flowed out carry out exchange heat water-cooled condenser 7, after cooling water absorption refrigeration agent liberated heat, temperature raises, flow out from coolant outlet 7b, domestic hot-water is provided.
The above is only preferred embodiment of the present utility model; be noted that for those skilled in the art; under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (9)
1. a heat pump driven dehumidification solution temperature controls and domestic hot-water's device for making, it is characterized in that: described device comprises heat pump assembly and solution humidifying device, described heat pump assembly comprises: frequency-changeable compressor (3), the four-way change-over valve (18) be connected by pipeline with frequency-changeable compressor (3), the solution cooler condenser (5) be connected by pipeline with four-way change-over valve (18), with solution cooler condenser (5) by pipeline and check-valves (17a), choke valve (4b), the water-cooled condenser (7) that check-valves (17b) is connected, with water-cooled condenser (7) by pipeline and choke valve (4a), check-valves (17c), the evaporimeter (6) that check-valves (17d) is connected, described evaporimeter (6) is connected by pipeline with four-way change-over valve (18), described solution humidifying device comprises: dehumidifier (1), the solution heat exchanger (10) be connected by pipeline and solvent valve with dehumidifier (1), the solution pump (8) be connected by pipeline with solution heat exchanger (10), the regenerator (2) be connected by pipeline with solution pump (8), the solution pump (9) that is connected by pipeline with solution heat exchanger (10), described regenerator (2) is connected by pipeline and solvent valve with solution heat exchanger (10), and described solution pump (9) is connected by pipeline with dehumidifier (1).
2. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: between solution cooler condenser (5) and evaporimeter (6), arrange water-cooled condenser (7) in heat pump, centre is connected by refrigerant tubing and valve.
3. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: water-cooled condenser (7) is provided with cooling water inlet (7a) and coolant outlet (7b), the pipeline between cooling water inlet (7a) and water-cooled condenser (7) is arranged water regulating valve (19).
4. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: the cooling water source in water-cooled condenser (7) is the tap water at normal temperature in local tap water pipe network.
5. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: the evaporimeter (6) in heat pump is connected with the dehumidifier (1) of solution humidifying system by pipeline, the solution cooler condenser (5) in heat pump is connected with the regenerator (2) of solution humidifying system by pipeline.
6. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: check-valves (17a) is connected with choke valve (4b) by pipeline, check-valves (17a) is in parallel with check-valves (17b), and circulating direction is contrary; Check-valves (17c) is connected with choke valve (4a) by pipeline, and check-valves (17c) is in parallel with check-valves (17d), and circulating direction is contrary.
7. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: the concentrated solution of solution heat exchanger (10) import and weak solution pipeline arrange solvent valve (11) and solvent valve (12) respectively.
8. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: the export pipeline of dehumidifier (1) arranges solvent valve (14), the export pipeline of regenerator (2) is arranged solvent valve (13).
9. heat pump driven dehumidification solution temperature according to claim 1 controls and domestic hot-water's device for making, it is characterized in that: described dehumidifier (1) and regenerator (2) arrange blower fan (15) and blower fan (16) respectively, correspondingly dehumidifier is arranged air blower import (1c) and air outlet slit (1d), regenerator (2) is arranged air intlet (2c) and air outlet slit (2d).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420799869.2U CN204513624U (en) | 2014-12-12 | 2014-12-12 | A kind of heat pump driven dehumidification solution temperature controls and domestic hot-water's device for making |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420799869.2U CN204513624U (en) | 2014-12-12 | 2014-12-12 | A kind of heat pump driven dehumidification solution temperature controls and domestic hot-water's device for making |
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| CN204513624U true CN204513624U (en) | 2015-07-29 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107869861A (en) * | 2016-09-23 | 2018-04-03 | 青岛海尔智能技术研发有限公司 | Plate type heat exchanger and heat pump |
| CN108224609A (en) * | 2018-01-23 | 2018-06-29 | 北京华创瑞风空调科技有限公司 | Solution humidifying device |
| CN109618688A (en) * | 2019-01-31 | 2019-04-16 | 中原工学院 | Low temperature drying damping multifunctional ecological grain storage system |
| CN110145830A (en) * | 2019-06-20 | 2019-08-20 | 南京工业大学 | A kind of wet independent process integration apparatus of air heat using solution dehumidification |
-
2014
- 2014-12-12 CN CN201420799869.2U patent/CN204513624U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107869861A (en) * | 2016-09-23 | 2018-04-03 | 青岛海尔智能技术研发有限公司 | Plate type heat exchanger and heat pump |
| CN108224609A (en) * | 2018-01-23 | 2018-06-29 | 北京华创瑞风空调科技有限公司 | Solution humidifying device |
| CN109618688A (en) * | 2019-01-31 | 2019-04-16 | 中原工学院 | Low temperature drying damping multifunctional ecological grain storage system |
| CN109618688B (en) * | 2019-01-31 | 2023-08-25 | 中原工学院 | Low-temperature drying and humidity-regulating multifunctional ecological grain storage system |
| CN110145830A (en) * | 2019-06-20 | 2019-08-20 | 南京工业大学 | A kind of wet independent process integration apparatus of air heat using solution dehumidification |
| CN110145830B (en) * | 2019-06-20 | 2024-03-05 | 南京工业大学 | Air heat and humidity independent treatment integrated equipment utilizing solution for dehumidification |
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Granted publication date: 20150729 Termination date: 20191212 |