CN201637017U - Heat pump hot and cold water supply device - Google Patents
Heat pump hot and cold water supply device Download PDFInfo
- Publication number
- CN201637017U CN201637017U CN2010201132683U CN201020113268U CN201637017U CN 201637017 U CN201637017 U CN 201637017U CN 2010201132683 U CN2010201132683 U CN 2010201132683U CN 201020113268 U CN201020113268 U CN 201020113268U CN 201637017 U CN201637017 U CN 201637017U
- Authority
- CN
- China
- Prior art keywords
- solution
- valve
- connects
- heat exchanger
- output
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Other Air-Conditioning Systems (AREA)
Abstract
The utility model relates to a heat pump hot and cold water supply device, which comprises a refrigerant loop and a solution loop, wherein the refrigerant loop comprises a compressor, a four-way valve, two heat exchangers, four one-way valves, two solenoid valves, a solution regenerator, a liquid reservoir, a filter, an electric expansion valve, a gas-liquid separator and related connecting pipes, and the solution loop comprises a cooling tower, three solenoid valves, a solution reservoir, a frequency conversion pump, an electric three-way adjusting valve, a solution regenerator, a second heat exchanger and related connecting pipes. The utility model solves the problems that the cold and hot sources of an air conditioning system have larger initial investment, a water-cooled chilling unit is idle in winter, an air source heat pump has lower refrigeration performance in summer (compared with the water-cooled chilling unit), and forms frost when running in winter, and is a solution water chilling and heating unit which can realize the water-cooled refrigeration in summer, adopts the cooling tower to realize the heating in winter, and utilizes the heat released from the super-cooling of the refrigerant as a solution regeneration heat source.
Description
Technical field
The utility model relates to a kind of summer and utilizes cooling tower to distribute condensation heat, utilize cooling tower winter, adopt solution to carry out heat exchange with air therein, solution absorbs heat as source heat pump heat, utilize cold-producing medium to cross cold refrigerating/heating method of emitting heat simultaneously as solution regeneration thermal source, and realize the device of this method, the technical field that belongs to the refrigerated air-conditioning system design and make.
Background technology
Along with the progressively exhaustion of fossil energy, energy problem has become the key factor of restriction global economy development.Along with improving constantly of rapid economy development and living standards of the people, the use of air conditioning system more and more widely becomes one of necessary condition of people's work and life, so air conditioning system is energy-conservation significant to alleviating energy shortage.
Building central air-conditioning Cooling and Heat Source scheme often adopts water-cooled handpiece Water Chilling Units+boiler at present, perhaps two kinds of schemes of air source heat pump.In first kind of scheme, summer the handpiece Water Chilling Units cooling, boiler is idle, winter boiler heat supplying, the water-cooled handpiece Water Chilling Units is idle.This scheme causes the idleness of equipment, and utilization rate is not high, and initial cost is bigger.In second kind of scheme, summer, air source heat pump was produced the cold water cooling, winter air source heat pump is also produced hot water heating simultaneously, realize dual-use, but when air source heat pump heats in the winter time simultaneously, there was the problem of evaporator surface frosting much smaller than the water-cooled handpiece Water Chilling Units in unit COP when air source heat pump freezed summer, the evaporator surface frosting not only reduces the COP of air source heat pump, and causes the safety and the reliability decrease of unit.
Therefore, it is bigger to solve existing building cold/heat supply scheme initial cost, the water-cooled handpiece Water Chilling Units idleness of equipment in winter waste, air source heat pump coefficient of performance of refrigerating in summer lower (with water-cooled handpiece Water Chilling Units ratio), there are problems such as frosting phenomenon in winter operation, designs a kind of new and effective water chiller/heater and consists of the technical barrier that those skilled in the art press for solution.
Summary of the invention
Technical problem: the purpose of this utility model is to reduce the initial cost of existing building cold/heat supply scheme, solve summer, the idleness of equipment in winter, utilization rate is low, improve the problem of air-conditioning system performance, propose to utilize cooling tower to distribute condensation heat a kind of summer, utilize cooling tower winter, adopt solution to carry out heat exchange with air therein, solution absorbs heat as thermal source, utilizes cold-producing medium to cross cold a kind of pump type heat hot and cold water feedway of emitting heat as solution regeneration thermal source simultaneously.
Technical scheme: a kind of pump type heat hot and cold water of the utility model feedway comprises refrigerant loop and solution loop.Refrigerant loop comprises compressor, cross valve, first heat exchanger, first check valve, second check valve, first magnetic valve, second magnetic valve, solution regenerator, reservoir, filter, electric expansion valve, the 3rd check valve, the 4th check valve, second heat exchanger, gas-liquid separator and relevant connection pipeline thereof.The output termination cross valve first input end 2a of compressor, the cross valve first output 2b meets the first input end 3a of first heat exchanger, the first output 3b of first heat exchanger connects first check valve inlet, the outlet of first check valve is divided into three the tunnel, the first via meets solution regenerator first input end 8a by first magnetic valve, and the solution regenerator first output 8b connects the input of reservoir; The second the tunnel also connects the input of reservoir by second magnetic valve; Third Road connects the outlet of second check valve, and the inlet of second check valve meets the first input end 14a of second heat exchanger.The output of reservoir connects the input of electric expansion valve by filter, the electric expansion valve output is divided into two-way, one the tunnel connects the inlet of the 4th check valve, the outlet of the 4th check valve meets the first input end 14a of second heat exchanger, other one the tunnel connects the inlet of the 3rd check valve, the outlet of the 3rd check valve meets the first output 3b of first heat exchanger, the first output 14b of second heat exchanger meets the second input 2c of cross valve, the second output 2d of cross valve connects the input of gas-liquid separator, and the input of the output termination compressor of gas-liquid separator; Solution loop comprises cooling tower, the 3rd magnetic valve, solution reservoir, the 4th magnetic valve, the 5th magnetic valve, variable frequency pump, electric three passes control valve, solution regenerator, second heat exchanger and relevant connection pipeline thereof.The cooling tower outlet is divided into two-way, and the 3rd magnetic valve of leading up to connects solution reservoir inlet, and the outlet of solution reservoir connects the inlet of variable frequency pump by the 5th magnetic valve; The 4th magnetic valve of leading up in addition also connects the inlet of variable frequency pump.The variable frequency pump outlet connects electric three passes control valve inlet, one way outlet of electric three passes control valve meets the second input 8c of solution regenerator, other one the tunnel meets the second input 14c of second heat exchanger after merging with the second output 8d of solution regenerator, and the second output 14d of second heat exchanger links to each other with the input port of cooling tower.
The utility model comprises two loops based on the solution type cold and hot water unit of cooling tower: refrigerant loop and solution loop.Concrete grammar of the present utility model is:
During based on the solution type cold and hot water unit refrigerating operaton in summer of cooling tower: refrigerant loop is that the refrigerant gas of low-temp low-pressure is sucked by compressor from gas-liquid separator, becoming the HTHP superheated vapor after the compression discharges, enter in second heat exchanger through cross valve, cold-producing medium is emitted heat, carry out condensation and become liquid, again successively through second check valve, first magnetic valve enters the solution regenerator, this moment, the solution regenerator played the effect of subcooler, liquid refrigerant carries out heat exchange with cooling water therein, refrigerant liquid temperature further reduces, and becomes subcooled liquid.After crossing cold cold-producing medium and coming out from the solution regenerator through becoming the gas-liquid two-phase of low-temp low-pressure behind reservoir, filter, the electric expansion valve, again through entering first heat exchanger behind the 3rd check valve, the cold-producing medium evaporation of in first heat exchanger, absorbing heat, produce cold water, becoming overheated gas after cold-producing medium evaporates fully comes out to enter gas-liquid separator through cross valve from first heat exchanger, and then be inhaled into compressor, thus finish kind of refrigeration cycle, produce cold water.All the other all are full of cooling water except that the solution reservoir in the solution loop at this moment, and solution is stored in the solution holder, does not participate in the circulation of solution loop.After cooling water comes out from cooling tower in solution loop, directly enter variable frequency pump by the 4th magnetic valve, after the variable frequency pump pressurization, cooling water enters the electric three passes control valve, the electric three passes control valve enters the solution regenerator with whole cooling waters, cooling water in the solution regenerator with the cold-producing medium heat exchange, the cooling refrigeration agent, make cold-producing medium cold excessively, cooling water temperature raises a little, and cooling water enters second heat exchanger after the solution regenerator comes out, absorb heat condensation of refrigerant is become liquid, enter cooling tower after self temperature further raises and carry out the wet exchange of heat, flow out like this circulation after cooling water temperature reduces once more from cooling tower with air.
During based on the operation of the solution type cold and hot water unit winter heating of cooling tower, refrigerant loop is to discharge through cross valve after the refrigerant gas of low-temp low-pressure in the gas-liquid separator is sucked, compresses by compressor to enter first heat exchanger, cold-producing medium is emitted heat in first heat exchanger, produce hot water, simultaneously self be condensed into liquid, after liquid refrigerant comes out from first heat exchanger, enter the solution regenerator through first check valve, first magnetic valve, cold-producing medium carries out heat exchange with solution therein, cold-producing medium is emitted heat, temperature reduces, and realizes cold.After crossing cold cold-producing medium and coming out from the solution regenerator, successively by reservoir, filter, electric expansion valve, entered in second heat exchanger through the 4th check valve with gas-liquid two-phase after the electric expansion valve throttling step-down, in second heat exchanger, evaporate heat absorption, cold-producing medium evaporates the back fully and enters gas-liquid separator from second heat exchanger cross valve that comes out to flow through, sucked, compress by compressor once more at last, so circulation.Charging solution in the solution loop this moment, solution enters the solution reservoir by the 3rd magnetic valve after cooling tower comes out, again through entering variable frequency pump behind the 5th magnetic valve, solution enters the electric three passes control valve after the variable frequency pump pressurization, solution is divided into two parts, a part enters the solution regenerator, solution is transpiring moisture therein, concentration improves, solution mixes with another part solution through the regeneration back, enters second heat exchanger, carries out heat exchange with cold-producing medium, emit heat, self temperature reduces, and solution enters cooling tower after second heat exchanger comes out, and (solution temperature is lower than air themperature to the solution of high concentration low temperature, the partial pressure of water vapor of solution is smaller or equal to airborne partial pressure of water vapor) in cooling tower, carry out the wet exchange of heat with air, solution absorbs heat from air, water in air steam condenses in solution, and the temperature of solution raises, concentration decreases, and flows out from cooling tower then to participate in circulation once more.
In the winter time during heating operation, solution carries out the wet exchange of heat with air in cooling tower, inevitably there is the problem of needs regeneration in solution, solution regeneration is meant that the moisture in the weak solution scatters and disappears from solution, make the concentration of solution improve, become concentrated solution, thereby have the ability that water in air is divided that absorbs once more.Conventional solution regeneration needs to use the thermal source of higher temperature (in the summer liquid desiccant air conditioning, because of environment temperature more than 30 ℃, the solution regeneration temperature requires more than 50 ℃), in the winter time, the hot and cold water unit need be produced hot water, the heat that will be higher than the hot water temperature is used for solution regeneration, will reduce the heating load of hot and cold water unit, and the heating performance of unit descends.The present invention adopts cold-producing medium to cross cold institute liberated heat to regenerate as solution that (environment temperature is generally below 15 ℃ during Winter heat supply for thermal source, the solution regeneration temperature gets final product for high 20 ℃ than ambient air temperature), not only realize regenerate low-gradeization of required thermal source of solution, simultaneously can realize that cold-producing medium is cold excessively, improve heating load and other performances of unit.Have energy-conservation and effect efficiently.
Beneficial effect:
1, a kind of pump type heat hot and cold water feedway that the utility model proposes can be realized water-cooled handpiece Water Chilling Units function in summer, compares the wind-cooled cold-water unit, has the higher coefficient of performance.Can realize producing hot water in the winter time, under same environment temperature, compare air source heat pump and have the higher coefficient of performance that the hot and cold water unit has been avoided inevitably frosting problem of air source heat pump institute simultaneously.
2, the solution type cold and hot water unit that the utility model proposes based on cooling tower, in the winter time during heating operation, adopt cold-producing medium to cross cold institute liberated heat, not only realized low-gradeization of solution regeneration thermal source, realized the cold excessively of cold-producing medium simultaneously as the regeneration thermal source.
3, the solution type cold and hot water unit based on cooling tower that the utility model proposes has solved original handpiece Water Chilling Units equipment idle problem in winter, has improved utilization rate of equipment and installations, has simplified the Cooling and Heat Source scheme of air conditioning system, has reduced initial cost.
Description of drawings
Accompanying drawing 1 is a kind of pump type heat hot and cold water of the utility model feedway schematic diagram.
Have among the above figure: compressor 1; Cross valve 2; Cross valve first input end 2a; The cross valve first output 2b; The cross valve second input 2c; The cross valve second output 2d; First heat exchanger 3; The first heat exchanger first input end 3a; First heat exchanger, the first output 3b; Cold or hot water inlet 31; Cold or hot water outlet 32; First check valve 4; Second check valve 5; First magnetic valve 6; Second magnetic valve 7; Solution regenerator 8; Solution regenerator first input end 8a; The solution regenerator first output 8b; The solution regenerator second input 8c; The solution regenerator second output 8d; Reservoir 9; Filter 10; Electric expansion valve 11; The 3rd check valve 12; The 4th check valve 13; Second heat exchanger 14; The second heat exchanger first input end 14a; Second heat exchanger, the first output 14b; Second heat exchanger, the second input 14c; Second heat exchanger, the second output 14d; Gas-liquid separator 15; Cooling tower 16; The 3rd magnetic valve 17; Solution reservoir 18; The 4th magnetic valve 19; The 5th magnetic valve 20; Variable frequency pump 21; Electric three passes control valve 22.
The specific embodiment
1 further specify the specific embodiment of the present utility model in conjunction with the accompanying drawings: a kind of pump type heat hot and cold water of the utility model feedway comprises refrigerant loop and solution loop; Concrete method of attachment is the first input end 2a of the output termination cross valve 2 of compressor 1, the first output 2b of cross valve 2 meets the first input end 3a of first heat exchanger 3, the first output 3b of first heat exchanger 3 connects the inlet of first check valve 4, the outlet of first check valve 4 is divided into three the tunnel, the first via meets solution regenerator first input end 8a by first magnetic valve 6, and the solution regenerator first output 8b connects the input of reservoir 9; The second the tunnel also connects the input of reservoir 9 by second magnetic valve 7; Third Road connects the outlet of second check valve 5, and the inlet of second check valve 5 meets the first input end 14a of second heat exchanger.The output of reservoir 9 connects the input of electric expansion valve 11 by filter 10, the output of electric expansion valve 11 is divided into two-way, one the tunnel connects the inlet of the 4th check valve 13, the outlet of the 4th check valve 13 meets the first input end 14a of second heat exchanger 14, another road connects the inlet of the 3rd check valve 12, the outlet of the 3rd check valve 12 meets first heat exchanger, the first output 3b, the first output 14b of second heat exchanger 14 meets the second input 2c of cross valve 2, the second output 2d of cross valve 2 connects the input of gas-liquid separator 15, and the input of the output termination compressor 1 of gas-liquid separator 15.
Summer is during refrigerating operaton: the low-temperature low-pressure refrigerant gas that comes out from gas-liquid separator 15 enters in second heat exchanger 14 through cross valve 2 by compressor 1 compression, after discharging, cold-producing medium and cooling water carry out heat exchange, condensation of refrigerant is emitted heat and is become liquid, enter solution regenerator 8 through second check valve 5, first magnetic valve 6 successively again, solution regenerator 8 plays the effect of subcooler at this moment, liquid refrigerant carries out heat exchange with cooling water therein, refrigerant liquid temperature further reduces, and becomes subcooled liquid.Become the gas-liquid two-phases of low-temp low-pressure after crossing cold cold-producing medium and coming out by throttling through reservoir 9, filter 10, electric expansion valve 11 backs from solution regenerator 8, again through entering first heat exchanger 3 behind the 3rd check valve 12, the cold-producing medium evaporation of in first heat exchanger 3, absorbing heat, produce cold water, becoming overheated gas after cold-producing medium evaporates fully comes out to enter gas-liquid separator 15 by cross valve 2 from first heat exchanger 3, be inhaled into compressor 1 once more and compress, finish kind of refrigeration cycle, produce cold water.All the other all are full of cooling water except that solution reservoir 18 in the solution loop at this moment, and solution is stored in the solution holder 18, does not participate in the circulation of solution loop.Cooling water is cooled in solution loop after tower 16 coolings, come out from cooling tower 16, directly enter variable frequency pump 21 (this moment, the 3rd magnetic valve 17 and the 5th magnetic valve 20 were closed) by the 4th magnetic valve 19, after variable frequency pump 21 pressurizations, cooling water enters electric three passes control valve 22, electric three passes control valve 22 enters solution regenerator 8 with whole cooling waters, cooling water in the solution regenerator 8 with the cold-producing medium heat exchange, the cooling refrigeration agent, make cold-producing medium cold excessively, cooling water temperature raises a little, cooling water enters after solution regenerator 8 comes out second heat exchanger 14, absorbs heat condensation of refrigerant is become liquid, enters cooling tower 16 after the further rising of self temperature and carries out the wet exchange of heat with air, after reducing, cooling water temperature flows out from cooling tower once more, so circulation.
Based on the operation of the solution type cold and hot water unit winter heating of cooling tower: the low-temperature low-pressure refrigerant steam of returning from gas-liquid separator 15 becomes the superheated vapor of HTHP after by compressor 1 compression, discharged process cross valve 2 by compressor 1 and enter first heat exchanger 3, cold-producing medium is emitted heat in first heat exchanger 3, produce hot water, simultaneously self be condensed into liquid, after liquid refrigerant comes out from first heat exchanger 3, through first check valve 4, first magnetic valve 6 (this moment, second magnetic valve 7 cut out) enters solution regenerator 8, cold-producing medium carries out heat exchange with solution therein, cold-producing medium is emitted heat, temperature reduces, and realizes cold.After crossing cold cold-producing medium and coming out from solution regenerator 8, successively by reservoir 9, filter 10, electric expansion valve 11, entered in second heat exchanger 14 through the 4th check valve 13 with gas-liquid two-phase after the electric expansion valve 11 throttling step-downs, in second heat exchanger 14, evaporate heat absorption, cold-producing medium evaporates the back fully and enters gas-liquid separator 15 from second heat exchanger 14 cross valve 2 that comes out to flow through, sucked, compress by compressor 1 once more at last, so circulation.Charging solution in the solution loop this moment, after coming out from cooling tower 16, solution enters solution reservoir 18 by the 3rd magnetic valve 17 (this moment, the 4th magnetic valve 19 cut out), again through entering variable frequency pump 21 behind the 5th magnetic valve 20, solution enters electric three passes control valve 22 after variable frequency pump 21 pressurizations, solution is divided into two parts, a part enters solution regenerator 8, solution is transpiring moisture therein, concentration improves, solution mixes with another part solution through the regeneration back, enters second heat exchanger 14, carries out heat exchange with cold-producing medium, emit heat, self temperature reduces, and solution enters cooling tower 16 after second heat exchanger 14 comes out, and (solution temperature is lower than air themperature to the solution of high concentration low temperature, the partial pressure of water vapor of solution is smaller or equal to airborne partial pressure of water vapor) in cooling tower 16, carry out the wet exchange of heat with air, solution absorbs heat from air, water in air steam condenses in solution, and the temperature of solution raises, concentration decreases, and flows out from cooling tower 16 then to participate in circulation once more.
Solution in cooling tower from air the key of draw heat be: the solution minimum temperature that 1, guarantee to participate in circulation is higher than the freezing point temperature of solution, thereby guarantee that solution solidification phenomenon can not occur in the operation of heat pump process, the present invention is by before regulating the operation of hot and cold water unit, and the solution concentration of injecting solution circulation loop can realize; 2, the solution temperature that enters cooling tower is lower than air themperature, thereby the assurance heat is passed to solution from air, the present invention regulates the liquid inventory that enters second heat exchanger by the frequency (promptly controlling the rotating speed of variable frequency pump) of control variable frequency pump, thereby guarantee that the solution temperature that enters cooling tower is lower than air themperature (when solution temperature is high, reduce liquid inventory, when solution temperature is too low, increase liquid inventory); 3, in the solution partial pressure of water vapor smaller or equal to airborne partial pressure of water vapor, make water vapour from air, enter solution, water recovery is emitted heat and is given solution (the partial pressure difference of water vapour is the driving force of water vapor diffusion), the size of partial pressure of water vapor depends on the concentration of solution in solution temperature one timing solution, and the concentration of control solution also just can realize the control of the partial pressure of water vapour in the solution.The present invention passes through control electric three passes control valve, regulates the liquid inventory that enters regenerator, thereby realizes the control to solution concentration, and solution concentration is than solution regeneration amount in hour increasing regenerator, and solution concentration reduces solution regeneration amount in the regenerator when big.
When winter heating operation switches to summer during refrigerating operaton, the solution in the solution loop all can be recovered in the solution reservoir, close the 3rd magnetic valve and the 5th magnetic valve after, again solution loop is filled water and gets final product.When summer refrigerating operaton switch to winter heating when operation, cooling water in original solution loop is drained, close the 4th magnetic valve, open the 3rd magnetic valve and the 5th magnetic valve, emit that solution gets final product in the solution reservoir.
Claims (1)
1. a pump type heat hot and cold water feedway is characterized in that this unit comprises refrigerant loop and solution loop; Refrigerant loop comprises compressor (1), cross valve (2), first heat exchanger (3), first check valve (4), second check valve (5), first magnetic valve (6), second magnetic valve (7), solution regenerator (8), reservoir (9), filter (10), electric expansion valve (11), the 3rd check valve (12), the 4th check valve (13), second heat exchanger (14), gas-liquid separator (15) and relevant connection pipeline thereof; The output termination cross valve first input end (2a) of compressor (1), cross valve first output (2b) connects the first heat exchanger first input end (3a), first heat exchanger, first output (3b) connects first check valve (4) inlet, the outlet of first check valve (4) is divided into three the tunnel, the first via connects solution regenerator first input end (8a) by first magnetic valve (6), and solution regenerator first output (8b) connects the input of reservoir (9); The second the tunnel also connects the input of reservoir (9) by second magnetic valve (7); Third Road connects the outlet of second check valve (5), and the inlet of second check valve (5) connects the second heat exchanger first input end (14a); The output of reservoir (9) connects the input of electric expansion valve (11) by filter (10), electric expansion valve (11) output is divided into two-way, one the tunnel connects the inlet of the 4th check valve (13), the outlet of the 4th check valve (13) connects the second heat exchanger first input end (14a), other one the tunnel connects the inlet of the 3rd check valve (12), the outlet of the 3rd check valve (12) connects first heat exchanger, first output (3b), second heat exchanger, first output (14b) connects cross valve second input (2c), cross valve second output (2d) connects the input of gas-liquid separator (15), and the input of the output termination compressor (1) of gas-liquid separator (15);
Solution loop comprises cooling tower (16), the 3rd magnetic valve (17), solution reservoir (18), the 4th magnetic valve (19), the 5th magnetic valve (20), variable frequency pump (21), electric three passes control valve (22), solution regenerator (8), second heat exchanger (14) and relevant connection pipeline thereof; Cooling tower (16) outlet is divided into two-way, and the 3rd magnetic valve (17) of leading up to connects solution reservoir (18) inlet, and the outlet of solution reservoir (18) connects the inlet of variable frequency pump (21) by the 5th magnetic valve (20); The 4th magnetic valve (19) of leading up in addition also connects the inlet of variable frequency pump (21).Variable frequency pump (21) outlet connects electric three passes control valve (22) inlet, one way outlet of electric three passes control valve (22) connects solution regenerator second input (8c), other one the tunnel connects second heat exchanger, second input (14c) after merging with solution regenerator second output (8d), and second heat exchanger, second output (14d) links to each other with the input port of cooling tower (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201132683U CN201637017U (en) | 2010-02-10 | 2010-02-10 | Heat pump hot and cold water supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201132683U CN201637017U (en) | 2010-02-10 | 2010-02-10 | Heat pump hot and cold water supply device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201637017U true CN201637017U (en) | 2010-11-17 |
Family
ID=43081512
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201132683U Expired - Fee Related CN201637017U (en) | 2010-02-10 | 2010-02-10 | Heat pump hot and cold water supply device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201637017U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101776353A (en) * | 2010-02-10 | 2010-07-14 | 东南大学 | Cooling tower-based solution type cold and hot water unit |
| CN103423815A (en) * | 2013-08-31 | 2013-12-04 | 湖南科技大学 | Solution-assistant energy-storage domestic air conditioner |
| CN116025972A (en) * | 2022-12-13 | 2023-04-28 | 福建省建筑设计研究院有限公司 | Integrated water loop multifunctional heat balancer |
-
2010
- 2010-02-10 CN CN2010201132683U patent/CN201637017U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101776353A (en) * | 2010-02-10 | 2010-07-14 | 东南大学 | Cooling tower-based solution type cold and hot water unit |
| CN103423815A (en) * | 2013-08-31 | 2013-12-04 | 湖南科技大学 | Solution-assistant energy-storage domestic air conditioner |
| CN103423815B (en) * | 2013-08-31 | 2015-07-29 | 湖南科技大学 | A kind of Solution-assistant energy-storage domestic air conditioner |
| CN116025972A (en) * | 2022-12-13 | 2023-04-28 | 福建省建筑设计研究院有限公司 | Integrated water loop multifunctional heat balancer |
| CN116025972B (en) * | 2022-12-13 | 2024-05-28 | 福建省建筑设计研究院有限公司 | Integrated water loop multifunctional heat balancer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100552323C (en) | The solar energy-air source energy-saving type solution heat pump device | |
| CN101776353A (en) | Cooling tower-based solution type cold and hot water unit | |
| CN100523652C (en) | Air source solution type heat pump device | |
| CN203231582U (en) | Two-stage compression heat pump system with economizer and defrosting by means of hot gas bypassing | |
| CN103148629B (en) | Gas-liquid phase ejector synergy refrigeration system for double temperature direct cooling-type refrigerator | |
| CN100533003C (en) | Air source solution heat pump device based on regeneration of reverse osmosis membrane solution | |
| CN203231419U (en) | Air conditioner | |
| CN203132224U (en) | Air conditioner | |
| CN106642789B (en) | Heat source tower heat pump system for realizing comprehensive utilization of solar energy and seasonal soil energy storage | |
| CN102022793B (en) | Latent heat recovery-based high-efficiency heat pump type heat source tower solution regenerating device and method | |
| CN102230686A (en) | Lithium bromide absorption-compression type series boosting refrigeration/heating pump system | |
| WO2015027573A1 (en) | Heat pump apparatus of heat source tower, for implementing low-pressure boiling regeneration of solution by using heat of subcooling | |
| CN103353189A (en) | Air-based heat-source tower heat pump for realizing high-efficiency utilization of regenerated heat based on air | |
| CN201293488Y (en) | Frosting free air source heat pump | |
| CN103411351A (en) | Heat-source tower heat pump for realizing solution regeneration and heat reutilization on basis of vacuum boiling | |
| CN103267325B (en) | Integrated heat source tower heat pump device based on comprehensive utilization | |
| CN203478691U (en) | Heat source tower heat pump system based on solution lower pressure boiling and regeneration | |
| CN110118448A (en) | Heat storage and cold accumulation type combustion gas assists solar absorption ammonium hydroxide cold supply system | |
| CN101413739A (en) | Double-effect heat pump circulation three-effect heat exchanger | |
| CN104729133A (en) | Double gas-liquid separator efficiency increasing and refrigerating circulating system for two-temperature direct-cooling refrigerator | |
| CN110701819B (en) | Three-working-condition system | |
| CN201149400Y (en) | Air source/water cold-hot pump device based on solution | |
| CN203605512U (en) | Air-cooling type compression condensing unit with supercooled gas-liquid separator | |
| CN106705494A (en) | Air source heat pump energy conservation system with function of preventing air side heat exchanger from freezing | |
| CN201637017U (en) | Heat pump hot and cold water supply device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101117 Termination date: 20140210 |