WO2014036744A1 - Dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais - Google Patents

Dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais Download PDF

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Publication number
WO2014036744A1
WO2014036744A1 PCT/CN2012/081215 CN2012081215W WO2014036744A1 WO 2014036744 A1 WO2014036744 A1 WO 2014036744A1 CN 2012081215 W CN2012081215 W CN 2012081215W WO 2014036744 A1 WO2014036744 A1 WO 2014036744A1
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WO
WIPO (PCT)
Prior art keywords
water
fresh air
atomizer
air
exhaust
Prior art date
Application number
PCT/CN2012/081215
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English (en)
Chinese (zh)
Inventor
房磊
袁舒
Original Assignee
上海朗诗建筑科技有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 上海朗诗建筑科技有限公司 filed Critical 上海朗诗建筑科技有限公司
Priority to CN201280075673.2A priority Critical patent/CN104704296A/zh
Priority to PCT/CN2012/081215 priority patent/WO2014036744A1/fr
Publication of WO2014036744A1 publication Critical patent/WO2014036744A1/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F3/147—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification with both heat and humidity transfer between supplied and exhausted air
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00—Control or safety arrangements
    • F24F11/30—Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
    • F24F11/46—Improving electric energy efficiency or saving
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00—Control or safety arrangements
    • F24F11/30—Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2110/00—Control inputs relating to air properties
    • F24F2110/20—Humidity
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
    • F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
    • F24F5/0035—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using evaporation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/54—Free-cooling systems

Definitions

  • the present invention relates to the field of building energy conservation, and is applicable to a heat recovery device used in a building ventilation system, and can effectively cool the exhaust air or heat in a building ventilation system.
  • the ground is passed to the fresh air to reduce the energy consumption of fresh air treatment.
  • the invention is particularly suitable for the occasion where the summer ventilation system needs to cool and dehumidify the fresh air, and the indoor air can be fully utilized for cooling and dehumidifying the fresh air.
  • Building energy consumption (including energy consumption in mining, ventilation, air conditioning, lighting, home appliances, office equipment and other power equipment), which accounts for more than 50% of global energy consumption, plays a vital role in energy conservation and emission reduction. Up to 30% of the building's energy consumption is used for ventilation, and this proportion is further enhanced with the widespread use of building insulation technology. Therefore, reducing the energy consumption of building ventilation is of great significance for energy conservation and emission reduction.
  • the air heat exchange technology for recovering sensible heat has been able to achieve more than 80% sensible heat recovery.
  • This technology is more effective for winter or dry heat summer climate, but for damp heat.
  • the sensible heat that can be recovered accounts for only 10-20% of the total heat energy consumption of the ventilation.
  • some of the efficiency is too low and the practical value is not large.
  • some can recover about 60% of the total heat energy consumption of ventilation due to the mass transfer of fresh air and exhaust air during the heat recovery process, a considerable part of the pollutants in the exhaust air are transmitted to the fresh air and sent back to the indoor with the fresh air. , thus making ventilation ineffective.
  • This heat recovery unit nominally recovers 60% of the total heat of ventilation, but in fact it also exacerbates indoor air pollution while doing heat recovery, which greatly reduces the effectiveness of ventilation (equivalent to a significant reduction in fresh air volume). The result is an increase in effective ventilation energy consumption, even worse than a ventilation system without heat recovery.
  • the Chinese utility model patent "an indirect evaporative fresh air ventilator” discloses a fresh air ventilating device, which is used in the air inlet and the cross flow type.
  • a humidifying device is arranged between the heat exchangers, so that the air discharged indoors to the outside is humidified to obtain a cooling temperature before entering the cross-flow heat exchanger, and the air cooled further is absorbed in the cross-flow heat exchanger and from the outside.
  • the incoming fresh air exchanges heat heat, which is beneficial to the outdoor air temperature to obtain a lower effect after the heat exchange.
  • the air discharged indoors to the outside is humidified and cooled by a shower water device before entering the heat exchanger.
  • the limit temperature at which air is cooled by such a cooling device is the wet bulb temperature of the air (unless the temperature of the water used for spraying is lower than the wet bulb temperature of the air).
  • the patent increases the temperature difference between the exhaust and the fresh air and increases the heat recovery, the effect of improving the heat recovery efficiency of the building ventilation in the hot and humid climate in summer is still very limited.
  • the reason is that the fresh air side cooling and condensation dehumidification
  • the total heat that needs to be released does not match the sensible heat absorbed by the temperature rise energy on the exhaust side.
  • the sensible heat absorbed by the temperature rise energy on the exhaust side is much lower than the total heat released by the fresh air side cooling and condensation and dehumidification.
  • the core problem to be solved by the present invention is the heat matching problem of heat exchange between fresh air and exhaust air, and the purpose thereof is to provide a total heat recovery device which effectively reduces the energy consumption of fresh air treatment, and the patent device can effectively heat the fresh air ( Including sensible heat and latent heat) is transmitted to the exhaust air to discharge the outside, so that the fresh air temperature and humidity are greatly reduced at the same time to reduce the cooling load of the ventilation system, and in the process, only heat transfer between the fresh air and the exhaust air does not have any mass transfer, thereby ensuring Fresh air is not contaminated by the heat recovery process.
  • a total heat recovery device that effectively reduces the energy consumption of fresh air treatment including:
  • An air heat exchanger a fresh air inlet, a fresh air outlet passing through the air heat exchanger and the fresh air inlet; a discharge air inlet, and a row passing through the air heat exchanger and the exhaust air inlet a wind outlet; the fresh air inlet and the exhaust outlet are located outdoors, the fresh air outlet and the exhaust inlet are located indoors; and an exhaust fan for guiding indoor air to the outside is disposed in the exhaust inlet.
  • a fresh air blower for guiding outdoor air into the room is disposed in the fresh air inlet; the device further includes a water atomization system for atomizing water into micron water droplets, the water atomization system including an atomization a water storage tank, one set in the row An atomizer between the air inlet and the air heat exchanger, a water pump for conveying water from the atomized water storage tank to the atomizer, a humidity sensor disposed in the air outlet, An atomization controller that controls a quantity of atomized water of the atomizer by a signal of the humidity sensor; the atomization controller controls an amount of atomized water of the atomizer such that a relative humidity at the exhaust outlet is maintained at 90 ⁇ 100%.
  • the function of the atomizer in this patent is to atomize water into micron-sized water droplets, which exchange heat with the air at the exhaust inlet, and evaporate and cool the water droplets to reduce the temperature of the exhaust air to the wet bulb temperature of the air.
  • the exhaust air is further humidified to a supersaturated state.
  • the micron-sized water droplets in the exhaust air evaporate rapidly due to the absorption of heat from the fresh air side, and because the exhaust air carries enough water mist, it can ensure that it has enough evaporation heat to satisfy the fresh air.
  • the heat of condensation required for side dehumidification, the heat exchange process in the air heat exchanger can be extended by the saturation line. This perfectly solves the heat matching problem of heat exchange between fresh air and exhaust air on both sides of the air heat exchanger.
  • the atomization controller controls the amount of atomized water of the atomizer such that the relative humidity at the exhaust outlet is kept infinitely close to or equal to 100%.
  • the atomizer atomizes water into water droplets having a diameter of 10 ⁇ m or less.
  • the air heat exchanger is a plate heat exchanger or a plate fin heat exchanger or a tube heat exchanger, and further, the plate heat exchanger is a counter flow plate heat exchanger or a fork plate heat Switch.
  • the atomizer is an ultrasonic atomizer or an air compression atomizer or a high pressure water atomizer, and still more preferably, the exhaust air inlet and the fresh air outlet are provided below A water tray for collecting condensed water and condensed water is connected, and the water tray is in communication with the atomizer tank.
  • the atomizer reservoir is provided with an overflow pipe for overflowing excess water in the atomizer reservoir.
  • the exhaust air entering the air heat exchanger must be humidified to a supersaturated state (ie, humidified to the fog area), and the water mist carried by the exhaust air should be in an appropriate amount, so as to ensure that the exhaust air is not separated from the air heat exchanger too early.
  • the saturation zone does not cause excessive atomization.
  • Its optimal exhaust air atomizing amount is the air
  • the relative humidity at the exhaust outlet of the heat exchanger is controlled to be infinitely close or to 100%. This allows the air treatment process as shown in Figure 1.
  • the water mist generated by the atomizer must be composed of water droplets having a diameter of 10 ⁇ m or less, so that the water mist can instantaneously evaporate heat in the air heat exchanger. To achieve higher heat recovery efficiency.
  • the water is atomized into micron-sized water droplets, so that the water droplets can fully evaporate the heat absorption, and at the same time, the atomizer is controlled to maintain a certain amount of atomized water spray.
  • the atomization water spray amount is too small to achieve the maximum evaporative cooling effect, so that the heat recovery efficiency is not maximized; when the atomization water spray amount is too large, the excess water mist cannot be Evaporation not only does not cool down, but also consumes a portion of the cooling for its own cooling, thereby reducing heat recovery efficiency while increasing water consumption.
  • the atomization spray quantity is controlled so that the relative humidity of the air outlet of the air heat exchanger reaches 90 to 100%, and the relative humidity is infinitely close to 100%.
  • the air treatment process shown in Figure 1 can be achieved when the relative humidity of the exhaust outlet is controlled to 100%. Otherwise, the atomizer's water addition is insufficient, so that the exhaust air is out of the fog area prematurely in the air heat exchanger (ie, supersaturated).
  • the indoor exhaust (state point A) is first cooled by the evaporation of water mist to the wet bulb temperature of the indoor air, and then heated with the fresh air along the saturation line (100% relative humidity line).
  • This patent is used in the climatic environment where the outdoor temperature in summer is higher than the indoor temperature and the outdoor is humid and humid.
  • the theoretical total heat recovery efficiency is over 100%, and the measured efficiency of the laboratory can reach 65% or higher (depending on indoor and outdoor climatic conditions). Depends on the performance of the air heat exchanger used).
  • this patented technology enables full heat recovery efficiency to be significantly higher than 100%.
  • the patented technology can partially or completely replace other refrigeration methods for fresh air cooling to reduce the room temperature to a comfortable range.
  • the total heat recovery efficiency is high, reaching and exceeding the most commonly used moisture absorption runner type full heat recovery device.
  • the structure is simple and easy to produce, low cost and easy to promote.
  • This patented device is easily retrofitted to existing air sensible heat recovery units.
  • the technology of the present invention can improve the total heat recovery efficiency. More than doubled, and the water consumption is greatly reduced, more energy-saving and environmentally friendly, and suitable for both winter and summer.
  • Figure 1 is a schematic illustration of the heat recovery principle of the present invention on a wetting diagram.
  • Figure 2 is a schematic view showing the structure of the apparatus of the present invention.
  • a total heat recovery device for effectively reducing the energy consumption of fresh air treatment includes: an air heat exchanger 1; a fresh air inlet 11, a fresh air outlet 12 through the air heat exchanger 1 and the fresh air inlet 11 ; an exhaust inlet 13 , an exhaust outlet 14 through the air heat exchanger 1 and the exhaust inlet 13; the fresh air inlet 11 and the exhaust outlet 14 are located outdoors, the fresh air outlet 12 and the exhaust inlet 13 are located indoors; An exhaust fan 16 for guiding indoor air to the outside is disposed in the inlet 13, and a fresh air fan 15 for guiding outdoor air into the room is disposed in the fresh air inlet 11; the patent device further includes a method for atomizing water into a water atomization system for micron-sized water droplets, the water atomization system comprising an atomized water storage tank 2, one disposed in the exhaust inlet 13 The atomizer 21, a water pump 24 for conveying water from the atomized water storage tank 2 to the atomizer 21, a humidity sensor 23 disposed in
  • the atomization controller 22 that controls the amount of atomized water of the atomizer 21; the atomization controller 22 controls the amount of atomized water of the atomizer 21 so that the relative humidity at the exhaust outlet 14 is maintained at 90 to 100%, if necessary With the optimum total heat recovery effect, the atomization controller 22 controls the amount of atomized water of the atomizer 21 such that the relative humidity at the humidity sensor 23 is maintained at or near 100%.
  • the amount of atomized water of the atomizer 21 is controlled so that the water mist can be quickly evaporated after being absorbed in the air heat exchanger 1 to achieve the heat recovery effect shown in Fig. 1.
  • the specific atomization water quantity control is to measure the relative humidity of the exhaust air outlet 14 (through the humidity sensor 23) to feed back the sensing signal to the atomization controller 22, and the atomization controller 22 controls the vibration of the ultrasonic atomizer vibrator.
  • the number is used to achieve precise atomization water volume control. This is one of the main features distinguishing the present invention from the prior art spray indirect evaporative cooler.
  • the air heat exchanger 1 is a plate heat exchanger or a plate fin heat exchanger or a tube heat exchanger, and preferably a counter flow plate type heat exchanger.
  • the air on both sides of the heat exchanger cannot leak from each other to prevent the heat recovery efficiency and the fresh air from being polluted by the exhaust air.
  • the atomizer 21 is an ultrasonic atomizer or an air compression atomizer or a high pressure water spray atomizer, and preferably an ultrasonic atomizer. Regardless of the structure of the atomization device, it is required to produce ultra-fine water mist of 10 microns or less. In this patent, the atomizer 21 produces a micron-sized water mist, and only an ultra-fine water mist can be quickly evaporated after absorption in the air heat exchanger 1 to achieve the heat recovery effect shown in Fig. 1. This is another major feature of the present invention that differs from prior art spray indirect evaporative coolers.
  • a drain tray 3 for collecting condensed water and condensed water is disposed below the exhaust air inlet 13 and the fresh air outlet 12, and the water tray 3 is connected with the atomizer water storage tank 2 to collect the collected condensed water and The condensate is recycled.
  • the atomizer tank 2 is provided with an overflow pipe 25 for overflowing excess water in the atomizer tank 2. This design drastically reduces the water consumption of the heat recovery unit of this patent.
  • the patented device can be further improved, such as setting a surface cooler at the fresh air outlet, so that the fresh air can be further cooled and dehumidified, at this time, on the fresh air cooler.
  • the condensed water can also be collected as a water supply to the atomizer 21.
  • the water required for the atomizer 21 of the present apparatus can be completely supplied by the condensed water on the fresh air side and the condensed water on the exhaust side without consuming additional water supply.
  • an air filter may also be provided at the fresh air inlet 11 to filter dust and particulate matter in the air, or a dedicated adsorption filter for removing gaseous pollutants in the air.
  • a water filtering device or a deionizing device may be disposed on the pipeline of the atomizer water storage tank 2 to the atomizer 21, so that the water entering the atomizer 21 can be cleaner and the atomization effect is more Well, the nebulizer has a longer maintenance-free period.
  • Table 1 shows the measured results obtained by testing the heat recovery performance of this patented device in a laboratory by simulating a group of summer extreme indoor and outdoor climates in East China.
  • the air heat exchanger 1 is a counter-current plate heat exchanger, and the experiment compares the total heat recovery efficiency of the patented device when the atomizer 21 is closed and opened. It can be seen from Table 1 that when the atomizer 21 is turned on and the relative humidity of the exhaust outlet of the heat recovery device is controlled to 100% by the atomization controller, the total heat recovery efficiency of the device of the present invention reaches 65%, when the fog is turned on.
  • the total heat recovery efficiency of the device of the present invention is 42% when the relative humidity of the exhaust outlet of the heat recovery device is controlled to 70% by the atomization controller, and the total heat recovery efficiency when the atomizer is turned off is only about 20 %, it can be seen that using the technology of the present invention and controlling the operation of the atomizer at the optimum atomization amount can substantially increase the total heat recovery efficiency of one counter current plate heat exchanger by more than two times. When the amount of atomization is insufficient, the total heat recovery efficiency will be significantly lower than the optimum value.
  • the air heat exchanger 1 is a countercurrent plate heat exchanger, and the experiment compares the total heat recovery efficiency of the patented device when the atomizer is turned off and on.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Atmospheric Sciences (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

L'invention porte sur un dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais, lequel dispositif comprend : un échangeur de chaleur air/air (1), une entrée d'air frais (11), une sortie d'air frais (12), une entrée d'air d'échappement (13), une sortie d'air d'échappement (14) et un système de pulvérisation d'eau qui pulvérise de l'eau sous la forme d'un brouillard de gouttelettes d'échelle micrométrique. Le système de pulvérisation d'eau comprend un réservoir d'eau pulvérisée (2), un pulvérisateur (21), une pompe à eau (24), un capteur d'humidité (23) disposé dans la sortie d'air d'échappement (14), et un dispositif de commande de pulvérisation (22). Le dispositif de commande de pulvérisation (22) commande la quantité d'eau pulvérisée du pulvérisateur (21) de façon à maintenir une humidité relative à la sortie d'air d'échappement (14) proche de 100 % ou égale à 100 %. Le dispositif de récupération de chaleur totale transfère efficacement la chaleur de l'air frais à un air d'échappement, et émet l'air d'échappement vers l'extérieur, ce qui réduit considérablement la température et l'humidité de l'air frais, de façon à réduire la charge de refroidissement d'un système de ventilation. Dans ce processus, seulement de la chaleur, mais non une masse d'air frais et d'air d'échappement, est transférée, empêchant de l'air frais d'être pollué dans le processus de récupération de chaleur.
PCT/CN2012/081215 2012-09-10 2012-09-10 Dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais WO2014036744A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201280075673.2A CN104704296A (zh) 2012-09-10 2012-09-10 一种有效降低新风处理能耗的全热回收装置
PCT/CN2012/081215 WO2014036744A1 (fr) 2012-09-10 2012-09-10 Dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2012/081215 WO2014036744A1 (fr) 2012-09-10 2012-09-10 Dispositif de récupération de chaleur totale réduisant efficacement une consommation d'énergie dans un traitement d'air frais

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WO2014036744A1 true WO2014036744A1 (fr) 2014-03-13

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CN (1) CN104704296A (fr)
WO (1) WO2014036744A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109059169A (zh) * 2018-09-21 2018-12-21 肖正广 逆流串联式高效节能新风机
DE102019109025A1 (de) * 2019-04-05 2020-10-08 Viessmann Werke Gmbh & Co Kg Vorrichtung zur Luftbefeuchtung
CN114838435A (zh) * 2021-02-02 2022-08-02 杭州瑞亚电气有限公司 转轮式热回收除湿净化新风系统

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5579949A (en) * 1978-12-13 1980-06-16 Sanyo Electric Co Ltd Total heat exchanger with supersonic humidifier
JPH01318821A (ja) * 1988-06-17 1989-12-25 Mitsubishi Electric Corp 間接式蒸発型冷房機
CN2075313U (zh) * 1990-08-07 1991-04-17 黄山 低能耗全新风供给空气调节器
CN1290837A (zh) * 1999-06-25 2001-04-11 胡光南 一种空气调节方法及装置
CN201819301U (zh) * 2010-10-05 2011-05-04 中南林业科技大学 一种智能温湿度控制装置

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1267682C (zh) * 2004-04-09 2006-08-02 袁一军 一种高效的气体全热回收和能量转换方法
CN101706135A (zh) * 2009-11-26 2010-05-12 万建红 雾化调温新风中央空调系统

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5579949A (en) * 1978-12-13 1980-06-16 Sanyo Electric Co Ltd Total heat exchanger with supersonic humidifier
JPH01318821A (ja) * 1988-06-17 1989-12-25 Mitsubishi Electric Corp 間接式蒸発型冷房機
CN2075313U (zh) * 1990-08-07 1991-04-17 黄山 低能耗全新风供给空气调节器
CN1290837A (zh) * 1999-06-25 2001-04-11 胡光南 一种空气调节方法及装置
CN201819301U (zh) * 2010-10-05 2011-05-04 中南林业科技大学 一种智能温湿度控制装置

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109059169A (zh) * 2018-09-21 2018-12-21 肖正广 逆流串联式高效节能新风机
DE102019109025A1 (de) * 2019-04-05 2020-10-08 Viessmann Werke Gmbh & Co Kg Vorrichtung zur Luftbefeuchtung
EP3734173A1 (fr) 2019-04-05 2020-11-04 Viessmann Werke GmbH & Co. KG Dispositif d'humidification d'air et méthode pour gérer ledit dispositif
CN114838435A (zh) * 2021-02-02 2022-08-02 杭州瑞亚电气有限公司 转轮式热回收除湿净化新风系统
CN114838435B (zh) * 2021-02-02 2023-08-22 杭州瑞亚电气有限公司 转轮式热回收除湿净化新风系统

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