CN201104060Y - Indirect evaporation type cooling/condensing unit - Google Patents
Indirect evaporation type cooling/condensing unit Download PDFInfo
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- CN201104060Y CN201104060Y CNU2007201905177U CN200720190517U CN201104060Y CN 201104060 Y CN201104060 Y CN 201104060Y CN U2007201905177 U CNU2007201905177 U CN U2007201905177U CN 200720190517 U CN200720190517 U CN 200720190517U CN 201104060 Y CN201104060 Y CN 201104060Y
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Abstract
The utility model relates to an indirect evaporative type cooling/ condensing device which comprises a blower, a shell, a spray thrower, a dividing wall type heat exchanger, an air inlet, a water pump and a water collecting tray; an air-water heat exchanger is arranged in the air inlet; the water pump pumps water from the water collecting tray and sends the water to a water passage of the air-water heat exchanger; ambient air imported from the air inlet is cooled, then enters the spray thrower; the water flows from the spray thrower, sprays on the outer surface of the dividing wall type heat exchanger and reflows to the water collecting tray by gravity; a cooled medium enters inside the dividing wall type heat exchanger from a cooled medium inlet and is cooled by the water sprayed from the spray thrower, then flows out from a cooled medium outlet. The utility model can be used as a closed type cooling tower and an evaporative type condenser; compared with the prior art, the indirect evaporative type cooling/ condensing device can make the liquid discharging temperature of the cooled monophasic fluid lower in summer, can also reduce the condensing temperature of the refrigerant and the chemical fluid system, operate in winter in a wind cooling mode, have the year-round cooling/condensing function and is favorable for the energy-saving operation of air conditioning, refrigeration and chemical systems.
Description
Technical field
The utility model relates to a kind of fluid cooling/condensing device that adopts the indirect evaporation mode, belongs to refrigeration, air-conditioning and chemical field, is specially adapted to evaporative condenser and closed cooling tower.
Background technology
Cooling tower is the cooling device commonly used of refrigeration, air-conditioning and chemical field, the high-temperature cooling water cooling that refrigeration machine can be discharged, produce cooling water a little more than air ' s wet bulb temperature, but conventional open type cooling tower is owing to directly contact with the external world, when system's long-time running, water quality deterioration, the salinity problems such as the water yield is big that concentrate, waft appear easily, life-span of refrigeration unit and efficient are all caused to a certain degree influence, be difficult to realize providing the function of zero cost chilled water (free cooling) simultaneously at low temperature season.
The appearance of closed cooling tower has well solved above-mentioned drawback, it adopts recuperator to realize the be cooled isolation of medium of evaporative cooling medium and refrigeration system, both guaranteed the be cooled quality of medium of refrigeration system, avoided blowing out of cooling mediums such as cooling water again, simultaneously can also be under the low temperature condition in the external world, stop the spray of cooling medium, only open the blower fan of cooling tower, can be converted into air-cooled cooling tower and produce the zero cost chilled water, make the air-conditioning system that needs cooling winter need not open handpiece Water Chilling Units and just can provide the idle call chilled water.The temperature of medium can only be reduced to more than the outside air temperature wet-bulb temperature but present closed cooling tower, employing recirculated water spray, cooling water etc. are cooled, and causes the efficient of the equipment such as handpiece Water Chilling Units of summer operation to reduce.
For providing temperature lower cooling water, China patent ZL02202739.4 discloses a kind of technical scheme that adopts the indirect evaporation mode to reduce the spray water temperature, realized that low cost produces the purpose of high temperature cold water, used the humiture independence control air conditioner system mode for dry area cheap low-temperature receiver is provided.But in this technical scheme, air directly contacts with the WATER AS FLOW MEDIUM that is cooled, and has the drawback of common open type cooling tower, particularly can not provide the zero cost chilled water under low temperature condition.
On the other hand, evaporative condenser is used widely in the cooling of high temperature refrigerant, chemical industry fluid, condensation process.Though evaporative condenser is under low temperature condition, by stopping the spray of cooling medium water, can be converted into air cooled condenser, but when summer operation, cooling/the condensation efficiency of evaporative condenser is subjected to the restriction of surrounding air wet-bulb temperature, the temperature of the medium that is cooled further can not be reduced.
In view of the foregoing, press for provide a kind of summer than the cooling effect of closed cooling tower and evaporative condenser is better, the medium temperature that is cooled is lower and the cooling of liquid phase fluids such as the water of the medium cooling function that still can realize winter being cooled, cold-producing medium, chemical industry fluid and/or the condensing unit of gaseous fluid, remedy the defective that present closed cooling tower and evaporative condenser exist.
The utility model content
Above-mentioned defective in view of present closed cooling tower and evaporative condenser existence, the purpose of this utility model will provide a kind of indirect evaporation type cooling/condensing device exactly, the liquid temp that goes out of the monophasic fluids that are cooled such as water is further reduced, prolong the service time of zero cost chilled water function, further reduce the condensation temperature of refrigeration system and chemical industry fluid system, realize the energy-saving run of air-conditioning, refrigeration and chemical system.
The technical scheme that realizes above-mentioned utility model purpose is as follows:
A kind of indirect evaporation type cooling/condensing device, this device comprise blower fan 1, housing 2, spray thrower 3, dividing wall type heat exchanger 4, water pump 6 and water-collecting tray 8; Described blower fan is arranged on the top of housing, described spray thrower is arranged on the top in the housing, dividing wall type heat exchanger is arranged on the bottom of spray thrower 3, be provided with air inlet 10 on the shell wall side below dividing wall type heat exchanger, described water-collecting tray is arranged on the bottom of housing, water-collecting tray 8 is provided with water supplement port 9, water-collecting tray is connected with water pump 6 inlets of water-collecting tray bottom by pipeline, water pump 6 outlets are connected with spray thrower 3 by pipeline, it is characterized in that: 10 places are provided with air-water-to-water heat exchanger 5 at described air inlet, and air-water-to-water heat exchanger water side joint is gone in the pipeline of water pump 6 and spray thrower 3.
In the utility model, described air-water-to-water heat exchanger should adopt symmetric arrangement.
Dividing wall type heat exchanger described in the utility model adopts the coil exchanger that is made of light pipe and/or finned tube.Around described dividing wall type heat exchanger, in the space filler 7 is set.This dividing wall type heat exchanger can adopt water or solution as cooling medium; Being cooled in the dividing wall type heat exchanger/cooling medium can be liquid, gas or two-phase fluid.
The utility model is owing to adopted technique scheme, the liquid temp that goes out of the monophasic fluids that are cooled such as water is further reduced, prolong the service time of zero cost chilled water function, further reduce the liquid temp that of the condensation temperature of refrigeration system and chemical industry fluid system and cold-producing medium, chemical industry fluid, realize the energy-saving run of air-conditioning, refrigeration and chemical system.
Be in particular in: 1. than the closed cooling tower of routine, the utility model can improve cooling effectiveness in summer under the prerequisite that increases cost slightly, and the liquid temp that goes out of the monophasic fluid that is cooled such as water is reduced; Under low outer warm environment, stop pump operation and spray thrower and spray, only move blower fan can realize the being cooled cooling purpose of monophasic fluid.Hence one can see that, further reduce the liquid temp that of the monophasic fluid that is cooled by the indirect evaporation cooling in summer, the monophasic fluid of low temperature was provided by indirect evaporation cooling or air cooling way in transition season and winter, reduced the running time of refrigeration machine, had practical value for the energy-saving run of systems such as air-conditioning, chemical industry; 2. for evaporative condenser, when adopting the technical solution of the utility model to make high-temperature gas or gas-liquid two-phase fluid condensation, the condensation temperature of refrigeration system and chemical industry cooling system is further reduced, to reduce the energy resource consumption of system in summer; Under the low temperature environment temperature, stop pump operation and spray thrower spray, only move blower fan and can realize the condensation of high-temperature gas or gas-liquid two-phase fluid, cold excessively purpose.
Cooling/the condensation effect of the indirect evaporation type cooling/condensing device that the utility model proposes when using summer is relevant with the relative humidity of surrounding air, humidity is low more, cooling effect is good more, so be particularly suitable for the usefulness of cooling/condensation of the single-phase or gas-liquid two-phase fluid in relatively dry area.
Description of drawings
The structure principle chart of the indirect evaporation type cooling/condensing device that Fig. 1 provides for the utility model.
The title of each parts is as follows among Fig. 1:
The 1-blower fan; The 2-housing; The 3-spray thrower; The 4-dividing wall type heat exchanger; 5-air-water-to-water heat exchanger; The 6-water pump; The 7-filler; The 8-water-collecting tray; The 9-water supplement port; The 10-air inlet; The 11-air draft; 12-is cooled/the condensed fluid inlet; 13-is cooled/the condensed fluid outlet.
The specific embodiment
The indirect evaporation type cooling/condensing device that the utility model provides can be used as closed cooling tower and evaporative condenser uses.Be further described below in conjunction with the 1 pair of concrete structure of the present utility model of accompanying drawing and the course of work.
Embodiment 1:
As shown in Figure 1, a kind of indirect evaporation type cooling/condensing device that the utility model provides, this device comprise blower fan 1, housing 2, spray thrower 3, dividing wall type heat exchanger 4, water pump 6 and water-collecting tray 8; Described blower fan is arranged on the top of housing, described spray thrower is arranged on the top in the housing, dividing wall type heat exchanger is arranged on the bottom of spray thrower 3, be provided with air inlet 10 on the shell wall side below dividing wall type heat exchanger, described water-collecting tray is arranged on the bottom of housing, water-collecting tray 8 is provided with water supplement port 9, and water-collecting tray is connected with water pump 6 inlets of water-collecting tray bottom by pipeline, and water pump 6 outlets are connected with spray thrower 3 by pipeline; 10 places are provided with air-water-to-water heat exchanger 5 at described air inlet, and air-water-to-water heat exchanger water side joint is gone in the pipeline of water pump 6 and spray thrower 3.
In the utility model, air-water-to-water heat exchanger can adopt two or more, should adopt symmetric arrangement.
Dividing wall type heat exchanger described in the utility model adopts the coil exchanger that is made of light pipe and/or finned tube.Around described dividing wall type heat exchanger, in the space filler 7 is set.This dividing wall type heat exchanger can adopt water or solution as cooling medium; Being cooled in the dividing wall type heat exchanger/cooling medium can be liquid, gas or two-phase fluid.
In above-mentioned indirect evaporation type cooling/condensing device, when the medium that is cooled in entering dividing wall type heat exchanger 4 was water, this device promptly can be used as the indirect evaporation closed cooling tower of air-conditioning system handpiece Water Chilling Units.Actual needs according to outside air temperature and system has following three kinds of operational modes:
(1) operational mode one: summer is during the handpiece Water Chilling Units refrigerating operaton, water pump 6 is opened, spray recirculated water, the cooling water that flows out from handpiece Water Chilling Units enters the aquaporin in the dividing wall type heat exchanger 4 through the medium inlet 12 that is cooled, heat sink to and reach cooling-down effect in the shower water, again through the media outlet 13 Returning water units that are cooled; Surrounding air passes through 5 precoolings of air-water-to-water heat exchanger earlier under the driving of blower fan 1, enter subsequently in the housing 2 with the shower water that has absorbed heat in dividing wall type heat exchanger 4 outsides or/and carry out directly in the filler 7 that heat is wet to be exchanged, shower water is lowered the temperature, it is interior recycling to fall into water-collecting tray 8 by gravity, and air is discharged housing 2 with hot and humid air draft 11 states; Water in the water-collecting tray 8 carries out moisturizing by water supplement port 9 again because of the part evaporation reduces gradually, and is constant to guarantee the water level in the water-collecting tray 8;
(2) operational mode two: still need under the operating mode of cooling in the not high but air-conditioning system of transition season outside air temperature, the water of dividing wall type heat exchanger 4 is directly switch in the chilled water loop of air-conditioning system, with the mode operation closed cooling tower of summer condition, thereby realize zero cost cooling cooling effect.
(3) operational mode three: when building still needs cooling in the winter time, if outside air temperature is enough low, on above-mentioned operational mode two bases, switch off the pump 6, stop the recirculated water spray, blower fan 1 still moves, and this moment, closed cooling tower was according to the air cooling heat exchanger mode operation, chilled water in the wall type heat exchanger 4 and outdoor air heat exchange cooling provide cold water to air-conditioning system.This air cooling way has been avoided the icing phenomenon of winter air-water-cooled heat exchange outside, can guarantee the cooling effect of safety and stability.
When the medium that is cooled in entering dividing wall type heat exchanger 4 was other liquid beyond the water, this device still was the indirect evaporation closed cooling tower, and the medium that is cooled is lowered the temperature effectively, and the closed cooling tower of its operational mode and cooling water is identical.
This shows, when technical solutions of the utility model are applied to closed cooling tower, than conventional closed cooling tower, under the prerequisite that increases cost slightly, can improve the cooling effectiveness of closed cooling tower in summer, the liquid temp that goes out of the monophasic fluid that is cooled such as water is reduced; Under low outer warm environment, stop water pump 6 runnings and spray thrower 3 and spray, only move blower fan 1 can realize the being cooled cooling purpose of monophasic fluid, reduced the running time of refrigeration machine, have practical value for the energy-saving run of systems such as air-conditioning, chemical industry.
Embodiment 2:
In the above-mentioned indirect evaporation type cooling/condensing device that the utility model provides, when adopting High Temperature Gas body such as cold-producing medium or gas-liquid two-phase fluid when the medium that is condensed in the dividing wall type heat exchanger 4, this device promptly can be used as the indirect evaporation type condenser of vapor compression type refrigerating system or chemical system.Because refrigeration system or chemical industry cooling system all need refrigeration throughout the year, so following two kinds of operational modes are generally arranged:
(1) operational mode one: under summer condition, water pump 6 is opened, and spray recirculated water enters High Temperature Gas body such as cold-producing medium in the dividing wall type heat exchanger 4 or gas-liquid two-phase fluid and heats sink to and reach condensation effect in the shower water.Outdoor air is under the driving of blower fan 1, earlier by 5 precoolings of air-water-to-water heat exchanger, enter subsequently in the housing 2 with the shower water that has absorbed heat in dividing wall type heat exchanger 4 outsides or/and carry out directly in the filler 7 that heat is wet to be exchanged, shower water is lowered the temperature, it is recycling to fall into water-collecting tray 8 by gravity, and air is discharged housing 2 with the air draft 11 of humid tropical condition.This process apparatus moves with the evaporative condenser state;
(2) operational mode two: if in the winter time to outside air temperature when enough low, switch off the pump 6, stop recirculated water spray, blower fan 1 normally move, makes High Temperature Gas body such as cold-producing mediums mobile in the dividing wall type heat exchanger 4 or gas-liquid two-phase fluid be condensed into liquid by air cooling way.This process apparatus moves with the air cooled condenser state.
As seen, when technical solutions of the utility model were applied to evaporative condenser, for existing evaporative condenser, the utility model can make the condensation temperature of refrigeration system and chemical industry cooling system further reduce in summer; Under the low temperature environment temperature, stop water pump 6 runnings and spray thrower 3 sprays, only moving blower fan 1 can be condensed into saturated high-temperature gas or gas-liquid two-phase fluid or subcooled liquid, can reduce the energy resource consumption of refrigeration system and chemical industry cooling system.
Claims (6)
1. indirect evaporation type cooling/condensing device, this device comprises blower fan (1), housing (2), spray thrower (3), dividing wall type heat exchanger (4), water pump (6) and water-collecting tray (8); Described blower fan is arranged on the top of housing, described spray thrower is arranged on the top in the housing, dividing wall type heat exchanger is arranged on the bottom of spray thrower (3), be provided with air inlet (10) on the shell wall side below dividing wall type heat exchanger, described water-collecting tray is arranged on the bottom of housing, water-collecting tray (8) is provided with water supplement port (9), water-collecting tray is connected with water pump (6) inlet of water-collecting tray bottom by pipeline, water pump (6) outlet is connected with spray thrower (3) by pipeline, it is characterized in that: locate to be provided with air-water-to-water heat exchanger (5) at described air inlet (10), air-water-to-water heat exchanger water side joint is gone in the pipeline of water pump (6) and spray thrower (3).
2. a kind of indirect evaporation type cooling/condensing device according to claim 1 is characterized in that: described air-water-to-water heat exchanger symmetric arrangement.
3. a kind of indirect evaporation type cooling/condensing device according to claim 1 is characterized in that: in the space filler (7) is being set around the described dividing wall type heat exchanger (4).
4. a kind of indirect evaporation type cooling/condensing device according to claim 1 is characterized in that: described dividing wall type heat exchanger (4) adopts the coil exchanger that is made of light pipe and/or finned tube.
5. a kind of indirect evaporation type cooling/condensing device according to claim 1 is characterized in that: described dividing wall type heat exchanger (4) adopts water or solution as cooling medium.
6. a kind of indirect evaporation type cooling/condensing device according to claim 1 is characterized in that: being cooled in the described dividing wall type heat exchanger (4)/cooling medium is liquid, gas or two-phase fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201905177U CN201104060Y (en) | 2007-11-30 | 2007-11-30 | Indirect evaporation type cooling/condensing unit |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201905177U CN201104060Y (en) | 2007-11-30 | 2007-11-30 | Indirect evaporation type cooling/condensing unit |
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| Publication Number | Publication Date |
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| CN201104060Y true CN201104060Y (en) | 2008-08-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2007201905177U Expired - Lifetime CN201104060Y (en) | 2007-11-30 | 2007-11-30 | Indirect evaporation type cooling/condensing unit |
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Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101392972B (en) * | 2008-10-29 | 2010-06-02 | 东南大学 | Synthesis water chilling unit based on evaporative cooling and vapour compression |
| CN102230654A (en) * | 2011-06-08 | 2011-11-02 | 于向阳 | Closed indirect evaporation water chiller |
| CN102242958A (en) * | 2011-06-08 | 2011-11-16 | 于向阳 | Closed type evaporating refrigeration cold water unit |
| CN103557643A (en) * | 2013-10-23 | 2014-02-05 | 珠海风合节能科技开发有限公司 | Condenser heat dissipation enhancing device for compression refrigerating machine and control method thereof |
| CN103604173A (en) * | 2013-11-21 | 2014-02-26 | 新疆绿色使者干空气能源有限公司 | Composite cooling device capable of being operated under multiple weather conditions |
| CN104048524A (en) * | 2014-06-18 | 2014-09-17 | 南通鸿景天机械设备科技有限公司 | Circulating water self-temperature reduction cooling device |
| CN104197745A (en) * | 2014-09-16 | 2014-12-10 | 中建三局第二建设工程有限责任公司 | Dry-wet combined cooling tower |
| CN104567453A (en) * | 2013-10-12 | 2015-04-29 | 湖北浠水蓝天联合气体有限公司 | Liquid nitrogen cold energy recovering system |
| CN104864519A (en) * | 2014-02-24 | 2015-08-26 | 禾玖科技股份有限公司 | Water energy conversion system |
| CN106052438A (en) * | 2016-06-25 | 2016-10-26 | 赖柱彭 | Piston type double-tube refrigerant heat dissipation exhaust gas spray tower |
| CN107842957A (en) * | 2017-10-19 | 2018-03-27 | 西安工程大学 | A kind of energy-saving efficient evaporation cooling handpiece Water Chilling Units of all-dimensional inlet |
| CN108106175A (en) * | 2017-12-12 | 2018-06-01 | 无锡市金来生物科技有限公司 | Crosswind sprinkle formula condenser |
| CN108278767A (en) * | 2018-02-07 | 2018-07-13 | 东北大学 | A kind of cooling/air-cooled heat exchange composite condenser of evaporation |
| CN109297119A (en) * | 2018-08-20 | 2019-02-01 | 黎庆佳 | A kind of cooling water-circulating energy-saving device of environment protection type air conditioner and round-robin method |
| CN110608492A (en) * | 2019-09-16 | 2019-12-24 | 珠海格力电器股份有限公司 | Precooling type evaporative condensation air-conditioning system and control method thereof |
| CN112879940A (en) * | 2021-02-22 | 2021-06-01 | 西安热工研究院有限公司 | Low-temperature flue gas latent heat recovery and comprehensive utilization system and method |
-
2007
- 2007-11-30 CN CNU2007201905177U patent/CN201104060Y/en not_active Expired - Lifetime
Cited By (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101392972B (en) * | 2008-10-29 | 2010-06-02 | 东南大学 | Synthesis water chilling unit based on evaporative cooling and vapour compression |
| CN102230654A (en) * | 2011-06-08 | 2011-11-02 | 于向阳 | Closed indirect evaporation water chiller |
| CN102242958A (en) * | 2011-06-08 | 2011-11-16 | 于向阳 | Closed type evaporating refrigeration cold water unit |
| CN102230654B (en) * | 2011-06-08 | 2013-09-18 | 于向阳 | Closed indirect evaporation water chiller |
| CN104567453A (en) * | 2013-10-12 | 2015-04-29 | 湖北浠水蓝天联合气体有限公司 | Liquid nitrogen cold energy recovering system |
| CN103557643A (en) * | 2013-10-23 | 2014-02-05 | 珠海风合节能科技开发有限公司 | Condenser heat dissipation enhancing device for compression refrigerating machine and control method thereof |
| CN103604173A (en) * | 2013-11-21 | 2014-02-26 | 新疆绿色使者干空气能源有限公司 | Composite cooling device capable of being operated under multiple weather conditions |
| CN104864519B (en) * | 2014-02-24 | 2017-07-14 | 禾玖科技股份有限公司 | water resource energy conversion system |
| CN104864519A (en) * | 2014-02-24 | 2015-08-26 | 禾玖科技股份有限公司 | Water energy conversion system |
| CN104048524A (en) * | 2014-06-18 | 2014-09-17 | 南通鸿景天机械设备科技有限公司 | Circulating water self-temperature reduction cooling device |
| CN104197745A (en) * | 2014-09-16 | 2014-12-10 | 中建三局第二建设工程有限责任公司 | Dry-wet combined cooling tower |
| CN104197745B (en) * | 2014-09-16 | 2017-01-25 | 中建三局第二建设工程有限责任公司 | Dry-wet combined cooling tower |
| CN106052438A (en) * | 2016-06-25 | 2016-10-26 | 赖柱彭 | Piston type double-tube refrigerant heat dissipation exhaust gas spray tower |
| CN107842957A (en) * | 2017-10-19 | 2018-03-27 | 西安工程大学 | A kind of energy-saving efficient evaporation cooling handpiece Water Chilling Units of all-dimensional inlet |
| CN108106175A (en) * | 2017-12-12 | 2018-06-01 | 无锡市金来生物科技有限公司 | Crosswind sprinkle formula condenser |
| CN108278767A (en) * | 2018-02-07 | 2018-07-13 | 东北大学 | A kind of cooling/air-cooled heat exchange composite condenser of evaporation |
| CN108278767B (en) * | 2018-02-07 | 2020-04-10 | 东北大学 | Evaporative cooling/air cooling heat exchange combined type condenser |
| CN109297119A (en) * | 2018-08-20 | 2019-02-01 | 黎庆佳 | A kind of cooling water-circulating energy-saving device of environment protection type air conditioner and round-robin method |
| CN109297119B (en) * | 2018-08-20 | 2021-01-08 | 枣庄市东行制冷设备有限公司 | Environment-friendly air conditioner refrigeration water circulation energy-saving device and circulation method |
| CN110608492A (en) * | 2019-09-16 | 2019-12-24 | 珠海格力电器股份有限公司 | Precooling type evaporative condensation air-conditioning system and control method thereof |
| CN110608492B (en) * | 2019-09-16 | 2023-12-15 | 珠海格力电器股份有限公司 | Precooling evaporative condensing air conditioning system and control method thereof |
| CN112879940A (en) * | 2021-02-22 | 2021-06-01 | 西安热工研究院有限公司 | Low-temperature flue gas latent heat recovery and comprehensive utilization system and method |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080820 |