CN105299794A - Double-channel cold and heat source haze purifying and heating tower - Google Patents
Double-channel cold and heat source haze purifying and heating tower Download PDFInfo
- Publication number
- CN105299794A CN105299794A CN201410343715.7A CN201410343715A CN105299794A CN 105299794 A CN105299794 A CN 105299794A CN 201410343715 A CN201410343715 A CN 201410343715A CN 105299794 A CN105299794 A CN 105299794A
- Authority
- CN
- China
- Prior art keywords
- heat
- tower body
- haze
- heat source
- cooling
- 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.)
- Granted
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a double-channel cold and heat source haze purifying and heating tower. The double-channel cold and heat source haze purifying and heating tower is composed of a bottom air inlet liquid film evaporation and cold purification system, an upper air inlet finned tube haze absorption heating system and a minus-temperature heat storage finned tube frost and haze removing system. The double-channel cold and heat source haze purifying and heating tower is characterized in that an openable air port of a low heat source is closed in summer, dry hot circulating air enters the surface of a water-cooling liquid film heat exchange layer through a lower air inlet grid, so that a liquid film is formed and evaporated, the outlet water temperature is low, and the cooling efficiency of a refrigerator is improved; drifting moisture is removed through a low heat source fin type heat exchanger, and loading and atmospheric circulation are achieved through driving of a draught fan; in winter, the openable air port of the low heat source is opened, a haze wet cold heat source directly releases low-temperature heat energy through freezing of the low heat source fin type exchanger, so that frost and haze removal can be conducted twice in a day cycle under the minus-temperature climate condition by means of 2% of stored heat energy of the heat source, and the low-temperature heat source having the atmospheric environment purification function is obtained to serve as a heat source of a heat pump.
Description
Technical field
The binary channels Cooling and Heat Source haze purification heat-obtaining tower 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 environmental protection technology, technology by the horizontal cooling tower of efficient for summer open type and winter high performance fin coil heat exchanger heat source tower unite two into one, retain respective performance advantage by two air channel.Utilize summer solar energy to transform the psychrometric difference air energy independent air intake grid produced, external water body liquid film evaporation cooler improves cryocooled efficiency; Utilizing winter the built-in circulatory mediator of horizontal finned coil pipe to absorb the clammy air of haze can as the thermal source of heat pump, haze air is purified while heat-obtaining, and adopt independently air inlet to reduce air circuit resistance, white haze is removed by negative temperature accumulation of heat energy secondary diurnal periodicity, 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%.
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 situation 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 directly forms the high efficiency of liquid film evaporation cooling in the tradition that summer retains at filling surface, 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, 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, this mode is confined in larger southern air-conditioning system.
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.The unified clear white haze system of large-scale accumulation of heat energy can be designed as big-and-middle-sized closed type heat source tower, but still need configuration accumulation of heat clear white haze system can just seem loaded down with trivial details as middle-size and small-size system.Special Problems existing is 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 in the medium and small architectural key applying heat source tower heat pump technical substitution fossil energy, technical requirement is the high efficiency that heat source tower should have the cooling of external filler spraying and sprinkling evaporation summer, the economic different transfer of heat in built-in circulation solution broadband low windage efficiency should be had winter, reduce while frosting probability raises the efficiency again, automatic clear white haze device should be had to realize atmospheric environment catharsis.
Summary of the invention
Type binary channels Cooling and Heat Source haze purification heat-obtaining tower object of the present invention.Be that closing low heat can blow in mouth summer, xeothermic circulating air enters water-cooled liquid film heat exchange layer surface by lower air intake grid and forms liquid film evaporation, leaving water temperature low raising cryocooled efficiency, removes drift moisture, through blower fan drive load and atmospheric air circulation by low heat finned heat exchanger; Be that opening low heat can blow in mouth winter, the clammy thermal source of haze is directly through low heat finned heat exchanger freezing absorption release low-temperature heat energy, under negative temperature weather conditions, remove white haze by can realize diurnal periodicity secondary to the accumulation of heat of thermal source (equipment absorb thermal source ability) 2%, 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, low heat finned heat exchanger is not heat exchange in the effect in summer, but be the anti-layer that wafts of Water spray cooling, 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, current China can be solved and there is no medium-sized horizontal two-channel Cooling and Heat Source haze purification heat-obtaining tower problem, realize the supporting of small and medium construction air-conditioning system heat source tower heat pump host application open and close type cold and heat source system.Binary channels Cooling and Heat Source haze purification heat-obtaining 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 end air intake liquid film evaporation cooling purification system 1; Upper air inlet finned tube inhales haze heat-obtaining system 2; Subzero temperature accumulation of heat clear finned tube frost haze system 3 forms.
Air intake liquid film evaporation cooling purification system of the described end 1, comprises by water cooling air intake grid, water-cooled liquid film heat exchange layer, water cooling liquid distribution, tee-joint guide valve group Y, tee-joint guide valve group Z, cooling water collecting device, low heat can blow in mouth, low heat finned heat exchanger, and air energy circulating fan forms.
Described water cooling air intake grid is installed between cooling water collecting device truss parallel with under tower body; Water cooling liquid film heat exchange layer is that horizontal type structure is inner between parallel truss with parallel truss lower in tower body under tower body, the all buckles of tower body tower body and tower body frame structure are fixed with water cooling liquid film heat exchange layer Special composition overall, cooling water collecting device is positioned at below water cooling liquid film heat exchange layer, above tower body sub-truss, water supplement port j is connected to outer water treatment feedwater, and delivery port k is connected with tee-joint guide valve group guide valve Y1 by pipeline; Water cooling liquid distribution in tower body lower parallel truss with in tower body on inner between parallel truss, water inlet is connected with tee-joint guide valve group guide valve Z1 by pipeline; Air energy circulating fan to be installed on tower body buckle top, aerophor lower portion on parallel truss, tower body, is and upper air inlet finned coil heat source tower device 2 shared device.
Described upper air inlet finned tube inhales haze heat-obtaining system 2, comprises and can be blown in mouth by low heat; Low heat finned heat exchanger, heat exchanger fin, heat exchanger coils, media expansion case, air energy circulating fan forms.
The described low heat mouth that can blow in be installed in tower body lower parallel truss and in tower body between upper parallel truss, holding opening winter is clammy thermal source air inlet, low heat finned tube exchanger is installed in tower body upper between parallel truss and media expansion case, the all buckles of tower body tower body and tower body frame structure are fixed with low heat finned tube exchanger Special composition overall, heat exchanger fin is risen by suit and connects interference fit and heat exchanger coils outside, heat exchanger coils D-2 import a is by pipeline and tee-joint guide valve group guide valve Z2, interface ZZ connects, b is by pipeline and tee-joint guide valve group guide valve Y2 in heat exchanger coils outlet, interface YY connects, media expansion case is installed between low heat finned tube exchanger truss parallel with on tower body, media expansion case fluid infusion mouth f is external liquid supplementation pipe, expansion interface e and heat exchanger coils export b and are connected, admission interface d is connected with heat exchanger coils import a, air energy circulating fan is installed on parallel truss on tower body, buckle top on tower body, aerophor lower portion, be and end air intake liquid film evaporation cooling tower device 1 shared device.
Described subzero temperature accumulation of heat clear finned tube frost haze system 3, comprise by subzero temperature 12h/2% electric heat-storage device, defrosting control valve group, temperature control equipment, defrosting circulating pump, low heat finned heat exchanger, heat exchanger fin, heat exchanger coils forms.
Described subzero temperature 12h/2% electric heat-storage device interface tz is connected by pipeline defrosting pump entry, defrosting circulating-pump outlet is connected with heat exchanger coils import a by pipeline, the two ends cross-over connection of defrosting control valve group has by-passing valve g, subzero temperature 12h/2% electric heat-storage device interface tw is connected with defrosting control valve group interface wb by pipeline, defrosting control valve group interface wa exports b by pipeline and heat exchanger coils and is connected, and subzero temperature 12h/2% electric heat-storage device interface we is connected to thermal source 2% electrothermal tube self-con-tained unit.
Accompanying drawing explanation
Fig. 1 is type one embodiment of the present invention " binary channels Cooling and Heat Source haze purification heat-obtaining tower " principle schematic;
Fig. 2 is type one embodiment of the present invention " end air intake liquid film evaporation cooling purification system " principle schematic;
Fig. 3 is type one embodiment of the present invention " upper air inlet finned tube inhales haze heat-obtaining system " principle schematic;
Fig. 4 is type one embodiment of the present invention " subzero temperature accumulation of heat clear finned tube frost haze system " principle schematic.
Detailed description of the invention
Below in conjunction with accompanying drawing: Fig. 1, Fig. 2, Fig. 3, Fig. 4 are described further type of the present invention " binary channels Cooling and Heat Source haze purification heat-obtaining tower " principle schematic.
With reference to accompanying drawing, the present embodiment comprises by end air intake liquid film evaporation cooling purification system 1; Upper air inlet finned tube inhales haze heat-obtaining system 2; Subzero temperature accumulation of heat clear finned tube frost haze system 3 forms.
Illustrate: figure hollow core arrow represents air-flow direction, filled arrows represents circulatory mediator, liquid, water circulation flow direction.
Air intake liquid film evaporation cooling purification system of the described end 1, comprises by water cooling air intake grid A-Y; Water-cooled liquid film heat exchange layer B-0, liquid film substrate B-1, liquid film wind chamber B-2; Water cooling liquid distribution C-0; Guide valve group Y; Guide valve group Z; Cooling water collecting device G-0; Low heat can blow in a mouthful A-Z; Low heat finned heat exchanger D-0; Air energy circulating fan F-0 is formed.
Described water cooling air intake grid A-Y is installed between cooling water collecting device G-0 truss 1-3 parallel with under tower body; Water cooling liquid film heat exchange layer B-0 is that horizontal type structure is inner between parallel truss 1-3 with parallel truss 1-4 lower in tower body under tower body, and tower body tower body week buckle 1-9 and tower body frame structure are fixed with water cooling liquid film heat exchange layer B-0 Special composition overall; Cooling water collecting device G-0 is positioned at below water cooling liquid film heat exchange layer B-0, above tower body sub-truss 1-1, and G-0 water supplement port j is connected to outer water treatment feedwater, and G-0 delivery port k is connected with tee-joint guide valve group Y guide valve Y1 by pipeline; Water cooling liquid distribution C-0 in tower body lower parallel truss 1-4 with in tower body on inner between parallel truss 1-5, C-0 water inlet is connected with tee-joint guide valve group Z guide valve Z1 by pipeline; Air energy circulating fan F-0 to be installed on tower body buckle 1-8 top on parallel truss 1-6, tower body, aerophor framework 1-7 is inner, is and upper air inlet finned coil heat source tower device 2 shared device.
Described upper air inlet finned tube inhales haze heat-obtaining system 2, comprises and can be blown in a mouthful A-Z by low heat; Low heat finned heat exchanger D-0, heat exchanger fin D-1, heat exchanger coils D-2; Media expansion case E-0; Air energy circulating fan F-0 is formed.
The described low heat mouthful A-Z that can blow in be installed in tower body between lower parallel truss 1-4 with parallel truss 1-5 upper in tower body, and holding opening winter is clammy thermal source air inlet; Low heat finned tube exchanger D-0 is installed in tower body upper between parallel truss 1-5 and media expansion case E-0, and tower body tower body week buckle 1-9 and tower body frame structure are fixed with low heat finned tube exchanger D-0 Special composition overall; Heat exchanger fin D-1 is risen by suit and connects interference fit and heat exchanger coils D-2 outside; Heat exchanger coils D-2 import a is connected with tee-joint guide valve group Z guide valve Z2, interface ZZ by pipeline, and heat exchanger coils D-2 is exported b and is connected with tee-joint guide valve group Y guide valve Y2, interface YY by pipeline; Media expansion case E-0 is installed between low heat finned tube exchanger D-0 truss 1-6 parallel with on tower body, media expansion case E-0 fluid infusion mouth f is external liquid supplementation pipe, and E-0 expansion interface e and heat exchanger coils D-2 export that b is connected, E-0 admission interface d is connected with heat exchanger coils D-2 import a; Air energy circulating fan F-0 to be installed on tower body buckle 1-8 top on parallel truss 1-6, tower body, aerophor framework 1-7 is inner, is and end air intake liquid film evaporation cooling tower device 1 shared device.
Described subzero temperature accumulation of heat clear finned tube frost haze system 3, comprises by subzero temperature 12h/2% electric heat-storage device H-0; Defrosting control valve group H-1; Temperature control equipment H-2; Defrosting circulating pump S-0; Low heat finned heat exchanger D-0, heat exchanger fin D-1, heat exchanger coils D-2 are formed.
Described subzero temperature 12h/2% electric heat-storage device H-0 interface tz is connected by pipeline defrosting circulating pump S-0 entrance; Defrosting circulating pump S-0 outlet is connected with heat exchanger coils D-2 import a by pipeline; Defrosting control valve group H-1 two ends cross-over connection has by-passing valve g; Subzero temperature 12h/2% electric heat-storage device H-0 interface tw is connected with defrosting control valve group H-1 interface wb by pipeline; Defrosting control valve group H-1 interface wa exports b by pipeline with heat exchanger coils D-2 and is connected; Subzero temperature 12h/2% electric heat-storage device H-0 interface we is connected to thermal source 2% electrothermal tube self-con-tained unit.
Binary channels Cooling and Heat Source haze purification heat-obtaining tower operation principle.
Binary channels Cooling and Heat Source haze purification heat-obtaining tower, by end air intake liquid film evaporation cooling purification system 1; Upper air inlet finned tube inhales haze heat-obtaining system 2; Subzero temperature accumulation of heat clear finned tube frost haze system 3 forms.
End air intake liquid film evaporation cooling purification system 1 operation principle, is shown in Fig. 1, Fig. 2.
Described closedown low heat can blow in a mouthful A-Z, close tee-joint guide valve group Y guide valve Y2, close tee-joint guide valve group Z guide valve Z2, open air energy circulating fan F-0.Cryocooled hot water enters water cooling liquid distribution C-0 through tee-joint guide valve group Z interface ZZ, guide valve Z1 and evenly sprays and rely on Action of Gravity Field to be covered with liquid film substrate B-1 on water cooling liquid film heat exchange layer B-0, the circulating air of relatively dry enters the evaporation and heat-exchange process that liquid film wind chamber B-2 forms liquid film surface, and hot water liquid film temperature reduces dependence Action of Gravity Field inflow cooling water collecting device G-0 and enters tee-joint guide valve group Y guide valve Y1, the interface YY cooling water as refrigeration machine via delivery port k; After opening air energy circulating fan F-0, the circulating air of relatively dry enters temperature rising after the B-2 heat exchange washing of water-cooled liquid film heat exchange layer B-0 liquid film wind chamber, humidity increase, dustiness decline through water cooling air intake grid A-Y, enter low heat finned tube exchanger D-0 and remove drift moisture, enter air energy circulating fan F-0 loaded cycle kinetic energy discharged to air.
Upper air inlet finned tube inhales haze heat-obtaining system 2 operation principle, sees Fig. 1, Fig. 3.
Described unlatching low heat can blow in a mouthful A-Z, close tee-joint guide valve group Y guide valve Y1, close tee-joint guide valve group Z guide valve Z1, open air energy circulating fan F-0.From the cryogenic freezing circulation solution of heat pump lower than air themperature more than 5 degree, through tee-joint guide valve group Z interface ZZ, guide valve Z2, enter low heat finned tube exchanger D-0, the clammy thermal source that heat exchanger fin D-1 absorbs in circulating air passes to heat exchanger coils D-2, cryogenic freezing circulation solution temperature raises enthalpy to be increased, and exports b, guide valve group Y guide valve Y2, interface YY as the low level heat source of heat pump via heat exchanger coils D-2; The clammy thermal source haze circulating air that relative humidity is larger after opening air energy circulating fan F-0 enters low heat finned tube exchanger D-0 and discharges that low temperature potential energy temperature declines, humidity reduces, dustiness declines enter air energy circulating fan F-0 loaded cycle kinetic energy to heat exchanger fin D-1 through the low heat mouthful A-Z that can blow in and complete the clammy thermal source absorption cleaning circulation of haze discharged to air.
Subzero temperature accumulation of heat clear finned tube frost haze system 3 operation principle, is shown in Fig. 1, Fig. 4.
Described ambient air temperature enters negative temperature, subzero temperature 12h/2% electric heat-storage device H-0 interface thermal source that we connects 2% electrothermal tube regulates subzero temperature 12h/2% electric heat-storage device H-0 pressure resistant vessel Inner eycle solution to 70 to spend left and right in temperature control equipment H-2 automatic control, the surrounding air negative temperature duration meets 12 hours, heat exchanger fin D-1 frosting thickness meets the requirement of defrosting haze, temperature control equipment H-2 exports and stops air energy circulating fan F-0 and heat pump run signal, open defrosting control valve group H-1, defrosting circulating pump S-0, subzero temperature 12h/2% electric heat-storage device H-0 hot solution enters defrosting circulating pump S-0 loaded cycle kinetic energy through H-0 interface tz, enter low heat finned heat exchanger D-0 heat exchanger coils D-2 release heat energy and pass to heat exchanger fin D-1, heat exchanger fin D-1 frost haze starts to melt, temperature control equipment H-2 detects that defrosting haze totally stops defrosting haze to run afterwards, System recover normal absorption haze heat-obtaining runs.
Claims (4)
1. binary channels Cooling and Heat Source haze purification heat-obtaining tower, comprise end air intake liquid film evaporation cooling purification system, upper air inlet finned tube inhales haze heat-obtaining system, subzero temperature accumulation of heat clear finned tube frost haze system composition, it is characterized in that: end air intake liquid film evaporation cooling purification system, upper air inlet finned tube inhales haze heat-obtaining system, subzero temperature accumulation of heat clear finned tube frost haze system.
2. binary channels Cooling and Heat Source haze purification heat-obtaining tower according to claim 1, air intake liquid film evaporation cooling purification system of the described end, is characterized in that: water cooling air intake grid is installed between cooling water collecting device truss parallel with under tower body; Water cooling liquid film heat exchange layer is that horizontal type structure is inner between parallel truss with parallel truss lower in tower body under tower body, and all buckles of tower body tower body and tower body frame structure are fixed with water cooling liquid film heat exchange layer Special composition overall; Cooling water collecting device is positioned at below water cooling liquid film heat exchange layer, above tower body sub-truss, water supplement port j is connected to outer water treatment feedwater, delivery port k is connected with tee-joint guide valve group guide valve Y1 by pipeline, water cooling liquid distribution in tower body lower parallel truss with in tower body on inner between parallel truss, water inlet is connected with tee-joint guide valve group guide valve Z1 by pipeline; Air energy circulating fan to be installed on tower body buckle top, aerophor lower portion on parallel truss, tower body, is and upper air inlet finned coil heat source tower device 2 shared device.
3. binary channels Cooling and Heat Source haze purification heat-obtaining tower according to claim 1, described upper air inlet finned tube inhales haze heat-obtaining system, it is characterized in that: the low heat mouth that can blow in be installed in tower body lower parallel truss and in tower body between upper parallel truss, holding opening winter is clammy thermal source air inlet, low heat finned tube exchanger is installed in tower body upper between parallel truss and media expansion case, the all buckles of tower body tower body and tower body frame structure are fixed with low heat finned tube exchanger Special composition overall, heat exchanger fin is risen by suit and connects interference fit and heat exchanger coils outside, heat exchanger coils D-2 import a is by pipeline and tee-joint guide valve group guide valve Z2, interface ZZ connects, b is by pipeline and tee-joint guide valve group guide valve Y2 in heat exchanger coils outlet, interface YY connects, media expansion case is installed between low heat finned tube exchanger truss parallel with on tower body, media expansion case fluid infusion mouth f is external liquid supplementation pipe, expansion interface e and heat exchanger coils export b and are connected, admission interface d is connected with heat exchanger coils import a, air energy circulating fan is installed on parallel truss on tower body, buckle top on tower body, aerophor lower portion, be and end air intake liquid film evaporation cooling tower device 1 shared device.
4. binary channels Cooling and Heat Source haze purification heat-obtaining tower according to claim 1, described subzero temperature accumulation of heat clear finned tube frost haze system, it is characterized in that: subzero temperature 12h/2% electric heat-storage device interface tz is connected by pipeline defrosting pump entry, defrosting circulating-pump outlet is connected with heat exchanger coils import a by pipeline, the two ends cross-over connection of defrosting control valve group has by-passing valve g, subzero temperature 12h/2% electric heat-storage device interface tw is connected with defrosting control valve group interface wb by pipeline, defrosting control valve group interface wa exports b by pipeline and heat exchanger coils and is connected, subzero temperature 12h/2% electric heat-storage device interface we is connected to thermal source 2% electrothermal tube self-con-tained unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410343715.7A CN105299794B (en) | 2014-07-19 | 2014-07-19 | The purification of binary channels Cooling and Heat Source haze takes thermal tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410343715.7A CN105299794B (en) | 2014-07-19 | 2014-07-19 | The purification of binary channels Cooling and Heat Source haze takes thermal tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105299794A true CN105299794A (en) | 2016-02-03 |
| CN105299794B CN105299794B (en) | 2018-06-01 |
Family
ID=55197362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410343715.7A Active CN105299794B (en) | 2014-07-19 | 2014-07-19 | The purification of binary channels Cooling and Heat Source haze takes thermal tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105299794B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107747782A (en) * | 2017-12-07 | 2018-03-02 | 青岛美克热源塔热泵研究有限公司 | A kind of high jet removes haze tower heat pump paddy electricity accumulation of energy cabin system |
| CN109925833A (en) * | 2019-04-16 | 2019-06-25 | 青岛美克热源塔热泵研究有限公司 | Low temperature refrigerating steam coring condensation removes haze tower |
| CN109974063A (en) * | 2019-04-16 | 2019-07-05 | 青岛美克热源塔热泵研究有限公司 | Suspended particulates freezing removes haze block chain energy source station |
| CN110145784A (en) * | 2019-06-12 | 2019-08-20 | 青岛美克热源塔热泵研究有限公司 | The absorption of assembled architecture refrigerating removes haze energy source station |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201327309Y (en) * | 2008-10-15 | 2009-10-14 | 上海汽车资产经营有限公司 | Open and close combined type multi-source double-effect energy tower |
| CN102003895A (en) * | 2010-11-24 | 2011-04-06 | 刘秋克 | Closed and integrated frostproof heat source tower |
| CN103499164A (en) * | 2013-08-12 | 2014-01-08 | 刘秋克 | Haze wet heat source heat pump water-cooling all-in-one machine |
| CN203595215U (en) * | 2013-11-26 | 2014-05-14 | 屹创能源工程（上海）有限公司 | Air-conditioner energy supply device |
| US20140338391A1 (en) * | 2013-03-15 | 2014-11-20 | Inertech Ip Llc | Multi-stage evaporative heat rejection process cycle that facilitates process cooling efficiency, water production, and/or water reclamation for fluid coolers and cooling towers |
-
2014
- 2014-07-19 CN CN201410343715.7A patent/CN105299794B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201327309Y (en) * | 2008-10-15 | 2009-10-14 | 上海汽车资产经营有限公司 | Open and close combined type multi-source double-effect energy tower |
| CN102003895A (en) * | 2010-11-24 | 2011-04-06 | 刘秋克 | Closed and integrated frostproof heat source tower |
| US20140338391A1 (en) * | 2013-03-15 | 2014-11-20 | Inertech Ip Llc | Multi-stage evaporative heat rejection process cycle that facilitates process cooling efficiency, water production, and/or water reclamation for fluid coolers and cooling towers |
| CN103499164A (en) * | 2013-08-12 | 2014-01-08 | 刘秋克 | Haze wet heat source heat pump water-cooling all-in-one machine |
| CN203595215U (en) * | 2013-11-26 | 2014-05-14 | 屹创能源工程（上海）有限公司 | Air-conditioner energy supply device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107747782A (en) * | 2017-12-07 | 2018-03-02 | 青岛美克热源塔热泵研究有限公司 | A kind of high jet removes haze tower heat pump paddy electricity accumulation of energy cabin system |
| CN109925833A (en) * | 2019-04-16 | 2019-06-25 | 青岛美克热源塔热泵研究有限公司 | Low temperature refrigerating steam coring condensation removes haze tower |
| CN109974063A (en) * | 2019-04-16 | 2019-07-05 | 青岛美克热源塔热泵研究有限公司 | Suspended particulates freezing removes haze block chain energy source station |
| CN110145784A (en) * | 2019-06-12 | 2019-08-20 | 青岛美克热源塔热泵研究有限公司 | The absorption of assembled architecture refrigerating removes haze energy source station |
| CN110145784B (en) * | 2019-06-12 | 2023-05-12 | 青岛美克热源塔热泵研究有限公司 | Cold absorption removes haze energy station is carried to assembled building |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105299794B (en) | 2018-06-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101846365B (en) | Solution dehumidifying fresh air unit using indoor exhaust evaporation cooling | |
| CN103712477B (en) | Heat pump heat supply demist water-saving cooling tower | |
| CN104197588B (en) | A kind of composite construction wet film surface cooler | |
| CN203672184U (en) | Heat pump heat-supply mist-removal water-saving type cooling tower | |
| CN206540334U (en) | Solar heat-preservation type air source heat pump defrosting system | |
| CN105698352B (en) | Solution regenerated summer in winter double efficiently heat source tower and heat-exchange methods are able to achieve using the sun | |
| CN201497390U (en) | Solar secondary biogenous cold-heat source tower | |
| CN105318461B (en) | The difunctional heat source tower of open and close type | |
| CN105299794A (en) | Double-channel cold and heat source haze purifying and heating tower | |
| CN203550703U (en) | Shaft air inlet preheating device | |
| CN101266104A (en) | Low energy consumption or entirely passive type heat quantity transfer device | |
| CN202885340U (en) | Energy supply device of high-efficiency energy tower | |
| CN106152766A (en) | A kind of dehumidification type heats thermal source | |
| CN203100472U (en) | Closed-type heat accumulating and cooling dual-purpose tower with defrosting function | |
| CN205261805U (en) | Evaporation formula condensing equipment based on separated heat pipe precooling | |
| CN212618913U (en) | Composite cooling tower and air conditioning system | |
| CN203501340U (en) | Heat pump type afterheat recovery fresh air handling unit | |
| CN202853065U (en) | Air conditioner defrosting circulation system | |
| CN209672864U (en) | The external dry and wet of heat exchanger combines closed cooling system | |
| CN106225334A (en) | A kind of vertically coiled pipe falling film evaporation condenser and method | |
| CN103398430A (en) | Heat-pump-type fresh air handing unit for waste heat recovery | |
| CN206207807U (en) | A kind of vertical coiled pipe falling film evaporation condenser | |
| CN104501321B (en) | A kind of inner-cooled solution dehumidification unit | |
| CN105318603B (en) | Commercial style open and close type heat source tower heat pump complexes | |
| CN204478367U (en) | All-weather solar water source heat pump air conditioning system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| CB02 | Change of applicant information |
Address after: 266300 Qingdao Research Institute, Huaihe Road, Jiaozhou economic and Technological Development Zone, Shandong 437, China Applicant after: Liu Qiuke Address before: 410007 Hunan province Changsha Yuhua District of Shaoshan City Road No. 489 Huambo Mingdi 3 room 1805 Applicant before: Liu Qiuke |
|
| COR | Change of bibliographic data | ||
| SE01 | Entry into force of request for substantive examination | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20160615 Address after: 811, room 6, 7 and 410000, Residence Internazionale, 568 Renmin Road, Changsha, Hunan Applicant after: Hunan three can steam heat pump Co.,Ltd. Address before: 266300 Qingdao Research Institute, Huaihe Road, Jiaozhou economic and Technological Development Zone, Shandong 437, China Applicant before: Liu Qiuke |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Room 2025, Building 1, Sunshine Jincheng, No. 35, Xinjian East Road, Shazitang Street, Yuhua District, Changsha City, Hunan Province, 410000 Patentee after: Hunan Sanheneng Engineering Co.,Ltd. Address before: Room 811, building 6 and 7, Rongsheng international apartment, 568 Renmin Middle Road, Changsha, Hunan 410000 Patentee before: Hunan three can steam heat pump Co.,Ltd. |