CN105318461A - Open-closed difunctional heat-source tower - Google Patents
Open-closed difunctional heat-source tower Download PDFInfo
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- CN105318461A CN105318461A CN201410248241.8A CN201410248241A CN105318461A CN 105318461 A CN105318461 A CN 105318461A CN 201410248241 A CN201410248241 A CN 201410248241A CN 105318461 A CN105318461 A CN 105318461A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000001816 cooling Methods 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 230000008020 evaporation Effects 0.000 claims abstract description 31
- 238000001704 evaporation Methods 0.000 claims abstract description 31
- 230000004087 circulation Effects 0.000 claims description 32
- 239000000498 cooling water Substances 0.000 claims description 18
- 239000012530 fluid Substances 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 9
- 239000011941 photocatalyst Substances 0.000 claims description 9
- 230000004089 microcirculation Effects 0.000 claims description 7
- 230000000740 bleeding effect Effects 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
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Abstract
The invention discloses an open-closed difunctional heat-source tower. The open-closed difunctional heat-source tower comprises an open-closed tower-type maintenance structure, a pneumatic heat exchange circulating system, a winter closed heat source system and a summer open cooling system. The open-closed difunctional heat-source tower is characterized in that in winter, broadband finned tube radiators of finned coil built-in media module groups are applied, a heat pump low-temperature level heat source which has a purification effect on the atmospheric environment is obtained to serve as a low-temperature level heat source of a heat pump; in summer, external water liquid film evaporative coolers are applied to directly conduct liquid film evaporation, and the cooling efficiency of a refrigerating machine is improved. By means of the open-closed difunctional heat-source tower, a cold or heat source is provided for achieving widespread application of a centenary single tube cooler upgrade heating pump of a large commercial air conditioner, carbon emission produced by fossil energy heat supply can be fully and efficiently replaced in a region with the air temperature below minus 15 DEG C, and carbon emission produced by fossil energy heat supply can be efficiently replaced by 30%-50% in a region with the air temperature above minus 15 DEG C.
Description
Technical field
The difunctional heat source tower of the open and close type that type of the present invention relates to relates to the large field of China's new energy source energy-saving technology, environmental protection and resource two.
New energy source energy-saving technology: by efficient for summer open type crossflow cooling tower and winter high-performance enclosed finned coil heat source tower unite two into one, retain respective performance advantage.Closed-type double action crank press function heat source tower utilizes solar energy to transform the psychrometric difference produced summer, and external water body liquid film evaporation cooler improves cryocooled efficiency; Utilizing winter finned coil built-in medium module group to absorb clammy haze air can as the thermal source of heat pump, economic environment-friend substitution fossil energy, contrasting conventional air source heat pump winter utilizes the clammy thermal source ability in air to improve more than 90%, summer system external water body liquid film evaporation cooler contrast hot blast cooling refrigeration energy-conservation more than 50%.
Environmental protection and resource: apply open and close type difunctional heat source tower winter and absorb the clammy thermal source of haze and originate as heat pump low level heat source, purify haze air while heat-obtaining.
Background technology
Along with the raising of people's living standard, the requirement of people to architectural environment is also more and more higher.Various refrigeration air-conditioner ventilates and heat supply process is promoted use day by day under construction, at current energy-saving low-carbon, reduce haze weather, under creating the large form of ecocity, green ecological district, green low-carbon building, the low-carbon environment-friendly energy-saving heating mode that heat source tower is originated as heat pump cold (heat) source, plays key player in the development of people's productive life.But in longtime running project investigation display:
Conventional open type heat source tower (similar open cooling tower structure), directly forms the high efficiency of liquid film evaporation cooling at filling surface in the tradition retained summer.But utilizing external circulation solution directly to absorb low level heat source at filling surface liquid film in the winter time, it is also more serious than Pollution of Boiler that matter melts process water capacity drift pollution corrosive environment metal.Utilize the clammy thermal source in frozen soln absorption air, solution is analysed wet dilution discharge and is caused certain water pollution, solution dilution causes solution concentration freezing point to rise simultaneously, and source pump frost heave damage phenomenon often occurs, and the loss of solution year accounts for more than 20% of Winter heat supply operating cost.
Novel closed type heat source tower also Shortcomings, utilize broadband low crammed Ji temperature difference finned tube exterior heat device by the circulating heat transfer to the clammy air of haze in the winter time, obtain the thermal source economic environmental protection of low level heat source as heat pump atmospheric environment to catharsis, do not have external circulation solution to the pollution of environment, frosting probability utilizes the energy in air to have dropped more than 90% than the highly dense fin heat pump of traditional large temperature difference.But in cooling in summer cooling procedure, need the meticulous maintenance of water treatment spraying and sprinkling evaporation cooling water being carried out to strict scale inhibition algae removal, once operation maintenance management is out of control, form jelly in incrustation scale+algae+air to cover finned tube surface and have a strong impact on heat-transfer effect and reach about 20%, lower cryocooled performance.
Thus solve and improve heat source tower heat pump technology, become the key applying heat source tower heat pump technical substitution fossil energy.Technical requirement heat source tower should have the high efficiency of external filler spraying and sprinkling evaporation cooling summer, built-in circulation solution should be had winter circulated by the economic different transfer of heat in broadband and air, then reduce the economy of acquisition to atmospheric environment catharsis while frosting probability is raised the efficiency.
Summary of the invention
The difunctional heat source tower object of type open and close type of the present invention.Be summer directly to utilize circulating water body to form liquid film evaporation at filling surface, improve the high efficiency of circulating water body cooling and resistant to pollution feature; Be winter to utilize economic temperature difference finned tube exterior heat device in broadband by the circulating heat transfer of air, obtain the thermal source of low level heat source as heat pump atmospheric environment to catharsis.
Contrast with conventional open type heat source tower, effectively can solve and absorb low level heat source winter, external circulation solution liquid-gas exchanges the matter process of melting and causes solution water capacity to be drifted about, contaminated environment corroding metal is than Pollution of Boiler also serious problems, and the loss of solution year accounts for more than 20% of Winter heat supply operating cost drops to lower than 2%, reach built-in circulation solution not dilute by heat-obtaining condensate water, solution concentration stablizes the security having ensured source pump.
Contrast with novel closed type heat source tower, effectively can solve the recirculated cooling water of summer without water treatment in the evaporative cooling of finned tube surface spraying, form jelly in incrustation scale+algae+air to cover finned tube surface and have a strong impact on heat-transfer effect and reach about 20%, reduce cryocooled performance issue.
Economy of the present invention, reasonably to run, the fatal shortcoming of current China heat source tower pump open cooling tower can be solved and closed type heat source tower finned coil vulnerable to pollution affects the performance issue caused.Open and close type difunctional heat source tower innovative technology can provide safe and reliable economy guarantee for heat source tower heat pump technology maturation.
The technical scheme of type of the present invention is: by the tower enclosed structure 1 of opening and closing, pneumatic recuperated cycle system 2, winter closed type heat source system 3, summer, open cooling system 4 formed.
The tower enclosed structure 1 of described opening and closing comprises tower body sub-truss; Cooling water water-collecting tray; Tower body column truss; Parallel truss on tower body; Aerophor truss; Tower body enclosed structure is formed.
Described tower body sub-truss upper end is connected and fixed by cooling water water-collecting tray and body disc and tower body column truss; Tower body sub-truss lower margin and basis are fixed; Tower body column truss truss parallel with on tower body is connected and fixed; Aerophor truss installa-tion is in tower body column truss top; Tower body enclosed structure is connected and fixed with tower body column truss, upper parallel truss respectively.
Described pneumatic recuperated cycle system 2: comprise photocatalyst air intake grid; External water body liquid film evaporation cooler; The built-in medium module group of finned coil; Pneumatic air heat-exchanger rig is formed.
Described photocatalyst air intake grid 2-1 is arranged in external water body liquid film evaporation cooler windward side; Finned coil built-in medium module group arrange with external water body liquid film evaporation cooler after and fix with tower body column truss structure; Pneumatic air heat-exchanger rig to be fixed on tower body above parallel truss structure.
Winter closed type heat source system 3: comprise triplet commutation cold flow valve; The built-in medium module group of finned coil; Triplet commutation heat source valve; Microcirculation expansion drum; Cooling and Heat Source circulation driving pump; Heat pump heat exchanger is formed.
Described triplet commutation cold flow valve outlet port is connected by feed tube on pipeline respectively medium module group built-in with both sides finned coil; In the built-in medium module group of both sides finned coil, feed tube extreme higher position is connected with circulation expansion drum microcirculation air bleeding valve A by pipeline; Under the built-in medium module group of both sides finned coil, drain pipe is connected with the import of triplet commutation heat source valve by pipeline; Under the built-in medium module group of finned coil, drain pipe lowest part is connected with circulation expansion drum interface B by pipeline; The outlet of triplet commutation heat source valve is connected with Cooling and Heat Source circulation driving pump entrance by pipeline; The outlet of Cooling and Heat Source circulation driving pump is connected with heat pump heat exchanger import; Heat pump heat exchanger outlet is connected with triplet commutation cold flow valve inlet by pipeline.
Summer open cooling system 4: comprise circulating water chennel in summer; Triplet commutation low-temperature receiver valve; Cooling and Heat Source circulation driving pump; Heat pump heat exchanger; Triplet commutation hot-fluid valve; Crossing current tower water drenching device; External water body liquid film evaporation cooler is formed.
Described summer, circulating water chennel was positioned at below cooling water water-collecting tray; Summer, circulating water chennel delivery port was connected with triplet commutation low-temperature receiver valve inlet by pipeline; Triplet commutation low-temperature receiver valve outlet port is connected with Cooling and Heat Source circulation driving pump entrance by pipeline; The outlet of Cooling and Heat Source circulation driving pump is connected with heat pump heat exchanger import by pipeline; Heat pump heat exchanger outlet is connected with triplet commutation hot-fluid valve inlet by pipeline; Triplet commutation hot-fluid valve outlet port is connected by pipeline and the both sides tower water drenching device that flows over; Crossing current tower water drenching device is installed on external water body liquid film evaporation cooler; External water body liquid film evaporation cooler is installed on above cooling water water-collecting tray.
Accompanying drawing explanation
Fig. 1 is type one embodiment of the present invention " the difunctional heat source tower of open and close type " enclosed heat-obtaining structural representation;
Fig. 2 is type one embodiment of the present invention " the difunctional heat source tower of open and close type " open type cooling structure schematic diagram.
Detailed description of the invention
Below in conjunction with accompanying drawing: enclosed heat-obtaining structural representation, open type cooling structure schematic diagram are described further respectively to type of the present invention " the difunctional heat source tower of open and close type " for Fig. 1, Fig. 2.
With reference to accompanying drawing, the present embodiment comprises by the tower enclosed structure 1 of opening and closing, pneumatic recuperated cycle system 2, winter closed type heat source system 3, summer, open cooling system 4 formed.
Illustrate: figure hollow core arrow represents air-flow direction, filled arrows represents circulatory mediator, liquid, water circulation flow direction.
The tower enclosed structure 1 of described opening and closing comprises tower body sub-truss 1-1; Cooling water water-collecting tray 1-2; Tower body column truss 1-3; Parallel truss 1-4 on tower body; Aerophor truss 1-5; Tower body enclosed structure 1-6 is formed.
Described tower body sub-truss 1-1 upper end is connected and fixed by cooling water water-collecting tray 1-2 and body disc and tower body column truss 1-3; Tower body sub-truss 1-1 lower margin and basis are fixed; Tower body column truss 1-3 truss 1-4 parallel with on tower body is connected and fixed; Aerophor truss 1-5 is installed on tower body column truss 1-3 top; Tower body enclosed structure 1-6 is connected and fixed with tower body column truss 1-3, upper parallel truss 1-4 respectively.
Described pneumatic recuperated cycle system 2: comprise photocatalyst air intake grid 2-1; External water body liquid film evaporation cooler G-1; The built-in medium module group G-2 of finned coil; Pneumatic air heat-exchanger rig 2-2 is formed.
Described photocatalyst air intake grid 2-1 is arranged in external water body liquid film evaporation cooler G-1 windward side; Finned coil built-in medium module group G-2 arrange with external water body liquid film evaporation cooler G-1 after and fix with tower body column truss structure; Pneumatic air heat-exchanger rig 2-2 is fixed on parallel truss 1-4 structure on tower body.
Winter closed type heat source system 3: comprise triplet commutation cold flow valve 3-1; The built-in medium module group G-2 of finned coil; Triplet commutation heat source valve 3-2; Microcirculation expansion drum P-1; Cooling and Heat Source circulation driving pump G-3; Heat pump heat exchanger G-4 is formed.
Described triplet commutation cold flow valve 3-1 outlet is connected by feed tube on pipeline respectively medium module group G-2 built-in with both sides finned coil; On the built-in medium module group G-2 of both sides finned coil, feed tube extreme higher position is connected with circulation expansion drum P-1 microcirculation air bleeding valve A by pipeline; Under the built-in medium module group G-2 of both sides finned coil, drain pipe is connected with triplet commutation heat source valve 3-2 import by pipeline; Under the built-in medium module group G-2 of finned coil, drain pipe lowest part is connected with circulation expansion drum P-1 interface B by pipeline; Triplet commutation heat source valve 3-2 outlet is connected with Cooling and Heat Source circulation driving pump G-3 entrance by pipeline; Cooling and Heat Source circulation driving pump G-3 outlet is connected with heat pump heat exchanger G-4 import; Heat pump heat exchanger G-4 outlet is connected with triplet commutation cold flow valve 3-1 entrance by pipeline.
Summer open cooling system 4: comprise circulating water chennel 4-1 in summer; Triplet commutation low-temperature receiver valve 4-2; Cooling and Heat Source circulation driving pump G-3; Heat pump heat exchanger G-4; Triplet commutation hot-fluid valve 4-3; Crossing current tower water drenching device 4-4; External water body liquid film evaporation cooler G-1 is formed.
Described summer, circulating water chennel 4-1 was positioned at below cooling water water-collecting tray 1-2; Summer, circulating water chennel 4-1 delivery port was connected with triplet commutation low-temperature receiver valve 4-2 entrance by pipeline; Triplet commutation low-temperature receiver valve 4-2 outlet is connected with Cooling and Heat Source circulation driving pump G-3 entrance by pipeline; Cooling and Heat Source circulation driving pump G-3 outlet is connected with heat pump heat exchanger G-4 import by pipeline; Heat pump heat exchanger G-4 outlet is connected with triplet commutation hot-fluid valve 4-3 entrance by pipeline; Triplet commutation hot-fluid valve 4-3 is exported and is connected by pipeline and the both sides tower water drenching device 4-4 that flows over; Crossing current tower water drenching device 4-4 is installed on external water body liquid film evaporation cooler G-1; External water body liquid film evaporation cooler G-1 is installed on above cooling water water-collecting tray 1-2.
The difunctional heat source tower structure function of open and close type and operation principle
The difunctional heat source tower of open and close type by the tower enclosed structure 1 of opening and closing, pneumatic recuperated cycle system 2, winter closed type heat source system 3, summer, open cooling system 4 formed.
Opening and closing tower enclosed structure 1 action principle, is shown in Fig. 1.
Described tower body sub-truss 1-1 tectonism, supports tower body armamentarium weight; Cooling water water-collecting tray 1-2 tectonism, collects external water body liquid film evaporation cooler G-1 evaporative cooling in summer recirculated water, finned coil built-in medium module group G-2 defrosting condensate water under collection negative temperature weather in winter; Tower body column truss 1-3 tectonism, supports parallel truss 1-4 and other truss on tower body and connects to form structural capacity group, fixing finned coil built-in medium module group G-2 equipment; Parallel truss 1-4 tectonism on tower body, supports aerophor truss 1-5; Tower body enclosed structure 1-6 tectonism, forms outer enclosed structure jointly with cooling water water-collecting tray 1-2.
Pneumatic recuperated cycle system 2 operation principle, is shown in Fig. 1.
The solar energy secondary source with infinite energy has been contained in air.Utilize summer solar energy to produce psychrometric difference, external water body liquid film evaporation cooler improves cryocooled efficiency; Improve heat exchanger cooling effectiveness, utilize winter the clammy haze air of finned coil built-in medium module group Inner eycle Absorption of Medium can as the thermal source of heat pump, economic environment-friend substitution fossil energy.
The pneumatic recuperated cycle of open type in summer: pneumatic air heat-exchanger rig 2-2 disturbance normal temperature low-humidity air circulation, external water body liquid film evaporation cooler G-1 is entered and liquid film evaporation cooler filling surface sprays liquid film forming evaporative cooling by photocatalyst air intake grid 2-1 crossing current, hot and humid air condition enters the outer fin layer of the built-in medium module group G-2 of finned coil, removing drift moisture is sucked by pneumatic air heat-exchanger rig 2-2, to be thrown to by hot and humid air again to enter photocatalyst air intake grid 2-1 after air carries out heat exchange and complete wet monsoon and move Thermal Cycling through blower fan driving.
The pneumatic recuperated cycle of enclosed in winter: the clammy air circulation of pneumatic air heat-exchanger rig 2-2 disturbance, enter external water body liquid film evaporation cooler G-1 by photocatalyst air intake grid 2-1 crossing current and remove dust in air and jelly, adverse current enters the built-in medium module group G-2 of finned coil and reduces to the finned coil release low temperature potential energy air status parameter temperature that changes, sucked by pneumatic air heat-exchanger rig 2-2, drive Low Temperature Wet cold air to throw to through blower fan and again to enter photocatalyst air intake grid 2-1 after air carries out heat exchange and complete dry monsoon and move Thermal Cycling.
Winter, closed type heat source system 3 operation principle, was shown in Fig. 1.
Enter finned coil built-in medium module group G-2 and clammy air from heat pump heat exchanger G-4 cryogen through triplet commutation cold flow valve 3-1 to circulate and form counter flow heat exchange process; Absorb and rise from the built-in medium temperature of the clammy thermal source finned coil in air, Cooling and Heat Source circulation driving pump G-3 loaded cycle energy is entered through triplet commutation heat source valve 3-2, enter heat pump heat exchanger G-4 and discharge the decline of sensible heat energy fluid temperature (F.T.), again enter cryogen and complete closed cycle in winter through triplet commutation cold flow valve 3-1.Microcirculation expansion drum P-1 principle is and System's composition microcirculation, and the system of playing stopped the automatic vent principle easily producing vapour lock for a long time.
Summer, open cooling system 4 operation principle, was shown in Fig. 2.
Cooling and Heat Source circulation driving pump G-3 loaded cycle energy is entered through triplet commutation low-temperature receiver valve 4-2 from circulating water chennel 4-1 cooling water in summer, enter heat pump heat exchanger G-4 and absorb the rising of sensible heat energy cooling water temperature, crossing current tower water drenching device 4-4 is entered through triplet commutation hot-fluid valve 4-3, high-temperature cooling water is evenly sprayed and forms liquid film by gravity at filling surface at external water body liquid film evaporation cooler G-1, normal temperature low humidity circulating air makes liquid film surface water molecule Pressure Drop low, the reduction of liquid film evaporation water temperature falls into cooling water water-collecting tray 1-2, enter summer circulating water chennel 4-1 and form inner evaporation cooling again.
Claims (4)
1. the difunctional heat source tower of open and close type, it comprises the tower enclosed structure of opening and closing, pneumatic recuperated cycle system, winter closed type heat source system, summer, open cooling system, is characterized in that pneumatic recuperated cycle system, winter closed type heat source system, summer open cooling system.
2. the difunctional heat source tower of open and close type according to claim 1, described pneumatic recuperated cycle system, it is characterized in that, photocatalyst air intake grid is arranged in external water body liquid film evaporation cooler windward side, finned coil built-in medium module group arrange with external water body liquid film evaporation cooler after and fix with tower body column truss structure, pneumatic recuperated cycle system to be fixed on tower body above parallel truss structure.
3. the difunctional heat source tower of open and close type according to claim 1 and 2, described closed type heat source system in winter, it is characterized in that, triplet commutation cold flow valve outlet port is connected by feed tube on pipeline respectively medium module group built-in with both sides finned coil, in the built-in medium module group of finned coil, feed tube extreme higher position is connected with circulation expansion drum microcirculation air bleeding valve A by pipeline, under the built-in medium module group of both sides finned coil, drain pipe is connected with the import of triplet commutation heat source valve by pipeline, under the built-in medium module group of finned coil, drain pipe lowest part is connected with circulation expansion drum interface B by pipeline, the outlet of triplet commutation heat source valve is connected with Cooling and Heat Source circulation driving pump entrance by pipeline, the outlet of Cooling and Heat Source circulation driving pump is connected with heat pump heat exchanger import, heat pump heat exchanger outlet is connected with triplet commutation cold flow valve inlet by pipeline.
4. the difunctional heat source tower of open and close type according to claim 1 or 2 or 3, described open cooling system in summer, it is characterized in that, summer, circulating water chennel was positioned at below cooling water water-collecting tray, summer, circulating water chennel delivery port was connected with triplet commutation low-temperature receiver valve inlet by pipeline, triplet commutation low-temperature receiver valve outlet port is connected with Cooling and Heat Source circulation driving pump entrance by pipeline, the outlet of Cooling and Heat Source circulation driving pump is connected with heat pump heat exchanger import by pipeline, heat pump heat exchanger outlet is connected with triplet commutation hot-fluid valve inlet by pipeline, triplet commutation hot-fluid valve outlet port is connected by pipeline and the both sides tower water drenching device that flows over, crossing current tower water drenching device is installed with on external water body liquid film evaporation cooler, external water body liquid film evaporation cooler is installed on above cooling water water-collecting tray.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810598038.1A CN108981038A (en) | 2014-06-06 | 2014-06-06 | The difunctional heat source tower of open and close type |
| CN201410248241.8A CN105318461B (en) | 2014-06-06 | 2014-06-06 | The difunctional heat source tower of open and close type |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410248241.8A CN105318461B (en) | 2014-06-06 | 2014-06-06 | The difunctional heat source tower of open and close type |
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| CN201810598038.1A Division CN108981038A (en) | 2014-06-06 | 2014-06-06 | The difunctional heat source tower of open and close type |
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| CN105318461A true CN105318461A (en) | 2016-02-10 |
| CN105318461B CN105318461B (en) | 2018-10-30 |
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| CN201810598038.1A Withdrawn CN108981038A (en) | 2014-06-06 | 2014-06-06 | The difunctional heat source tower of open and close type |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105627628A (en) * | 2016-03-21 | 2016-06-01 | 潘燕 | Heat source tower chemical heat pump |
| CN108266832A (en) * | 2018-02-06 | 2018-07-10 | 贵州电网有限责任公司 | A kind of compound outdoor heat exchange device of solution-type antifrost |
| CN109798615A (en) * | 2019-01-25 | 2019-05-24 | 东南大学 | A kind of transverse flow type heat source tower based on phase-change microcapsule solution |
| CN109990619A (en) * | 2019-01-28 | 2019-07-09 | 北京朗博科科技发展有限公司 | Heat exchanger external dry and wet joint closed cooling system and cooling means |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110410891B (en) * | 2019-07-11 | 2021-04-16 | 山东摩卡智能科技有限公司 | Air purification system with dredging function by adopting photocatalyst technology |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101270941A (en) * | 2008-05-21 | 2008-09-24 | 刘秋克 | Heat source tower heat pump |
| CN101672552A (en) * | 2009-10-12 | 2010-03-17 | 湖南秋克热源塔热泵科技工程有限公司 | Tower heating pump complete device with solar energy secondary heat source |
| CN201497096U (en) * | 2009-09-27 | 2010-06-02 | 湖南秋克热源塔热泵科技工程有限公司 | Damp-heat energy negative pressure cooling refrigerator |
| US20100242517A1 (en) * | 2009-03-27 | 2010-09-30 | Bryce Johnson | Solar Photovoltaic Closed Fluid Loop Evaporative Tower |
| CN102003838A (en) * | 2010-11-16 | 2011-04-06 | 刘秋克 | Solar-powered primary source heat source tower heat pump complete device |
-
2014
- 2014-06-06 CN CN201410248241.8A patent/CN105318461B/en active Active
- 2014-06-06 CN CN201810598038.1A patent/CN108981038A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101270941A (en) * | 2008-05-21 | 2008-09-24 | 刘秋克 | Heat source tower heat pump |
| US20100242517A1 (en) * | 2009-03-27 | 2010-09-30 | Bryce Johnson | Solar Photovoltaic Closed Fluid Loop Evaporative Tower |
| CN201497096U (en) * | 2009-09-27 | 2010-06-02 | 湖南秋克热源塔热泵科技工程有限公司 | Damp-heat energy negative pressure cooling refrigerator |
| CN101672552A (en) * | 2009-10-12 | 2010-03-17 | 湖南秋克热源塔热泵科技工程有限公司 | Tower heating pump complete device with solar energy secondary heat source |
| CN102003838A (en) * | 2010-11-16 | 2011-04-06 | 刘秋克 | Solar-powered primary source heat source tower heat pump complete device |
Non-Patent Citations (1)
| Title |
|---|
| 张晨等: "三种典型结构热源塔的比较", 《制冷与空调》 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105627628A (en) * | 2016-03-21 | 2016-06-01 | 潘燕 | Heat source tower chemical heat pump |
| CN108266832A (en) * | 2018-02-06 | 2018-07-10 | 贵州电网有限责任公司 | A kind of compound outdoor heat exchange device of solution-type antifrost |
| CN108266832B (en) * | 2018-02-06 | 2023-12-01 | 贵州电网有限责任公司 | Solution type frosting prevention compound outdoor heat exchange device |
| CN109798615A (en) * | 2019-01-25 | 2019-05-24 | 东南大学 | A kind of transverse flow type heat source tower based on phase-change microcapsule solution |
| CN109990619A (en) * | 2019-01-28 | 2019-07-09 | 北京朗博科科技发展有限公司 | Heat exchanger external dry and wet joint closed cooling system and cooling means |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105318461B (en) | 2018-10-30 |
| CN108981038A (en) | 2018-12-11 |
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