CN201138102Y - A new return air energy recovery heat pump device with a secondary humidification cooling condenser - Google Patents
A new return air energy recovery heat pump device with a secondary humidification cooling condenser Download PDFInfo
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- CN201138102Y CN201138102Y CN200720310534.XU CN200720310534U CN201138102Y CN 201138102 Y CN201138102 Y CN 201138102Y CN 200720310534 U CN200720310534 U CN 200720310534U CN 201138102 Y CN201138102 Y CN 201138102Y
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- 238000001816 cooling Methods 0.000 title claims abstract description 30
- 238000011084 recovery Methods 0.000 title description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000000034 method Methods 0.000 claims description 15
- 238000009833 condensation Methods 0.000 claims description 13
- 230000005494 condensation Effects 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 10
- 239000011521 glass Substances 0.000 claims description 3
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 2
- 229910052731 fluorine Inorganic materials 0.000 claims description 2
- 239000011737 fluorine Substances 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 3
- 238000001914 filtration Methods 0.000 claims 3
- 230000008676 import Effects 0.000 claims 2
- 230000000712 assembly Effects 0.000 claims 1
- 238000000429 assembly Methods 0.000 claims 1
- 238000005057 refrigeration Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 230000003020 moisturizing effect Effects 0.000 abstract 4
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 230000007423 decrease Effects 0.000 abstract 1
- 238000004378 air conditioning Methods 0.000 description 9
- 238000007791 dehumidification Methods 0.000 description 9
- 238000001704 evaporation Methods 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000003905 indoor air pollution Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
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- 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]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
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Abstract
Description
技术领域 technical field
本实用新型涉及一种带二次加湿冷却式冷凝器的新回风能量回收热泵装置,对被冷凝器加热的空气利用蒸发器凝结水进行加湿降温处理,再次经过下一级冷凝器对与高温制冷剂换热,创造性地用热泵实现了新排风的全热回收,属于制冷机组及空调处理过程技术领域。The utility model relates to a new return air energy recovery heat pump device with a secondary humidification and cooling condenser, which uses the condensed water of the evaporator to perform humidification and cooling treatment on the air heated by the condenser, and then passes through the next-stage condenser to meet the high temperature again. Refrigerant heat exchange creatively uses a heat pump to realize full heat recovery of new exhaust air, and belongs to the technical field of refrigeration units and air conditioning treatment processes.
背景技术 Background technique
新排风热回收作为降低建筑设备能耗的重要方法已经为空调技术领域所重视,且目前已经在国内有大量的推广应用。但是目前的几种主要的热回收方式方法及设备,均存在着应用方面的重大问题,因此实际工程中成功落实的项目远未达到所期望的目标。例如目前的板式新排风热交换器一般只进行显热交换,实现全热交换的产品存在有机换热元件会产生病菌、异味,两类热回收器都存在总体上效率较低,尺寸较大,风组过大导致风机能耗大,结露及冬季结霜问题难以有效解决,长期使用时积累大量灰尘导致污染严重,成本较高等缺点;转轮式热回收器尺寸过大、价格过高等;其它如新排风分别与水换热并通过循环管路传热及热管式等往往只能实现显热交换,且存在运行控制复杂、冬季需避免水管冻裂冻坏等问题。上述原因均导致了新排风热回收实际应用上的能效比、经济性、可操作性等困难,严重影响到这一重要节能技术的实际推广。As an important method to reduce the energy consumption of building equipment, the heat recovery of new exhaust air has been paid attention to in the field of air conditioning technology, and has been widely promoted and applied in China. However, there are major problems in the application of several main heat recovery methods and equipment at present, so the projects successfully implemented in actual projects are far from reaching the expected goals. For example, the current plate-type new exhaust air heat exchanger generally only performs sensible heat exchange, and the products that realize full heat exchange have organic heat exchange elements that will generate germs and odors. Both types of heat recovery devices have low overall efficiency and large size. , the wind group is too large, which leads to high energy consumption of the fan, the problem of condensation and winter frost is difficult to effectively solve, and the accumulation of a large amount of dust during long-term use leads to serious pollution and high cost. ; Others such as the new exhaust air respectively exchange heat with water and transfer heat through the circulation pipeline and the heat pipe type can only achieve sensible heat exchange, and there are problems such as complicated operation control and the need to avoid freezing and cracking of water pipes in winter. The above-mentioned reasons have led to difficulties in the practical application of new exhaust air heat recovery, such as energy efficiency ratio, economy, and operability, which have seriously affected the actual promotion of this important energy-saving technology.
将热泵应用于新排风热回收也是一种重要方法,但是目前风冷冷凝器的能效比一般比较低,仅能达到3.0或稍多,与板式及转轮式机组通常宣传可达到6以上相比过低,这种性能指标使热泵难以成为新排风热回收的主要手段。特别是制冷系统的特点是冷凝热量一般高出蒸发冷量10~30%左右,而通常冷凝器的内外传热温差一般低于蒸发器,且冷凝器冷却空气的进出口温差通常比蒸发器被冷却空气要小,这对风冷冷风型制冷机组一般会造成冷凝风量比蒸发风量高出30~100%以上。而通常空调系统的有组织排风量要低于新风量10%左右,那么当将热泵应用于新排风热回收时,若仅仅吸收排风中有限的显热量,则对新风的冷却除湿能力较低,无法充分发挥热泵热回收的优势。Applying heat pumps to new exhaust air heat recovery is also an important method, but the energy efficiency ratio of air-cooled condensers is generally relatively low at present, and can only reach 3.0 or slightly more, which is comparable to that of plate and rotary units that can reach above 6. The ratio is too low, this performance index makes it difficult for the heat pump to become the main means of heat recovery from fresh exhaust air. In particular, the characteristic of the refrigeration system is that the heat of condensation is generally 10-30% higher than the cooling capacity of evaporation, and the temperature difference between the inside and outside of the condenser is generally lower than that of the evaporator, and the temperature difference between the inlet and outlet of the cooling air of the condenser is usually higher than that of the evaporator. The cooling air should be small, and the air-cooled cold air type refrigeration unit generally causes the condensing air volume to be 30-100% higher than the evaporating air volume. Usually, the organized exhaust air volume of the air conditioning system is about 10% lower than the fresh air volume, so when the heat pump is applied to the heat recovery of the new exhaust air, if only the limited sensible heat in the exhaust air is absorbed, the cooling and dehumidification capacity of the fresh air will be greatly reduced. Low, unable to take full advantage of the heat recovery of the heat pump.
当用于空调系统的冬季加湿时,由于热泵冷凝部分只能实现显热加热,则必须另设一套加湿器,增加了结构尺寸及成本。When it is used for humidification of air conditioning system in winter, since the condensing part of the heat pump can only realize sensible heat heating, another set of humidifier must be installed, which increases the structure size and cost.
目前空调系统空气处理过程普遍采用冷冻除湿方法,空气的降温、除湿过程耦合,将制冷机的蒸发温度降到很低水平以满足除湿需要,导致制冷机能效比大幅下降,增加初投资及运行费用。At present, the air treatment process of the air conditioning system generally adopts the refrigeration dehumidification method. The cooling of the air and the dehumidification process are coupled to reduce the evaporation temperature of the refrigerator to a very low level to meet the dehumidification needs, resulting in a significant drop in the energy efficiency ratio of the refrigerator, increasing the initial investment and operating costs. .
发明内容 Contents of the invention
本实用新型的目的和任务是,针对上述存在的种种问题,根据空气含湿量不变时温度越高吸湿能力越强的特性,创造性的对被冷凝器加热的空气进行加湿处理,使其温度沿近似等焓过程降低到很低温度,再次经过下一级冷凝器与高温制冷剂换热,水源则为可认为不含钙镁离子的蒸发器凝结水,从而实现了将蒸发器凝结水所含冷量全部或部分的回收利用,避免了直接采用自来水加湿导致的结垢问题,且冷凝器所需风量减少了50%以上,创造性的用热泵实现了新排风的全热回收,且全热效率可接近100%,在室外空气温度不很高时由于排风温度远超室外气温而使全热效率超过100%,远远超过目前所有新排风热回收的效率,节能效益十分显著。The purpose and task of this utility model is to solve the various problems mentioned above, according to the characteristic that the higher the temperature is, the stronger the moisture absorption capacity will be when the moisture content of the air is constant, creatively humidify the air heated by the condenser to make its temperature It is lowered to a very low temperature along the approximate isenthalpic process, and then passes through the next-stage condenser to exchange heat with the high-temperature refrigerant. The water source is the condensed water of the evaporator that can be considered to contain no calcium and magnesium ions, thus realizing the condensed water of the evaporator. The recycling of all or part of the cooling capacity avoids the fouling problem caused by the direct use of tap water for humidification, and the air volume required by the condenser is reduced by more than 50%. The thermal efficiency can be close to 100%. When the outdoor air temperature is not very high, the total thermal efficiency exceeds 100% because the exhaust air temperature is far higher than the outdoor air temperature, far exceeding the heat recovery efficiency of all new exhaust air at present, and the energy-saving benefit is very significant.
为此,本实用新型设计了一种带二次加湿冷却式冷凝器的新回风能量回收热泵装置,由压缩机、冷凝器、蒸发器、膨胀阀、四通阀、单向阀组、储液器、干燥过滤器、汽液分离器及其它配件组成,其中冷凝器分为三级热湿处理过程,第一级将室内排风由室温20~26℃左右冷凝加热处理到40~50℃,第二级将排风加湿冷却到20~26℃左右,第三级再将排风由冷凝器加热到45~50℃并排向室外。一、三级冷凝器采用翅片式换热器,二级加湿器采用超声波加湿器或者雾化喷淋加湿器。若必要,还可在第三级之后再设置四级加湿冷却器和五级冷凝加热器。For this reason, the utility model designs a new return air energy recovery heat pump device with a secondary humidification cooling condenser, which consists of a compressor, a condenser, an evaporator, an expansion valve, a four-way valve, a one-way valve group, a storage The condenser is divided into three-stage heat and humidity treatment process. The first stage condenses and heats the indoor exhaust air from room temperature of 20-26°C to 40-50°C. , The second stage humidifies and cools the exhaust air to about 20-26°C, and the third stage heats the exhaust air to 45-50°C by the condenser and discharges it to the outside. The first and third stage condensers use finned heat exchangers, and the second stage humidifiers use ultrasonic humidifiers or atomized spray humidifiers. If necessary, a fourth-stage humidifying cooler and a fifth-stage condensing heater can be installed after the third stage.
夏季处理过程的加湿水源为蒸发器凝结水,从而实现基本上把新风冷却除湿后的凝结水所含冷量利用热泵进行回收的目标,即完成了全热回收过程,且不浪费自来水水源。The humidification water source in the summer treatment process is the evaporator condensate water, so as to achieve the goal of basically recovering the cooling capacity contained in the condensate water after the fresh air cooling and dehumidification by using the heat pump, that is, the full heat recovery process is completed, and tap water is not wasted.
通常的转轮式或板式等热回收器对于新风除湿过程而言仅仅是被动除湿过程,无法实现有效控制除湿水平,而采用本实用新型的热泵热回收装置,完全可实现冷冻独立除湿,这对空调系统而言具有如下重大意义:中央空调系统的制冷主机将冷冻水出水温度由通常的7℃左右大幅度提升到15℃左右,则中央空调制冷机组的能效比大幅提高,制冷机及空调系统相关设备部件的容量较大幅度降低,初投资及运行费用较大幅度下降,且可实现室内风机盘管的干式运行,彻底解决了由于风盘接水盘内大量滋生有害微生物导致的室内空气污染及空调病。For the fresh air dehumidification process, the usual wheel-type or plate-type heat recovery device is only a passive dehumidification process, which cannot effectively control the dehumidification level. However, the heat pump heat recovery device of the present utility model can completely realize freezing and independent dehumidification. For the air-conditioning system, it has the following great significance: the cooling host of the central air-conditioning system will greatly increase the chilled water outlet temperature from about 7°C to about 15°C, and the energy efficiency ratio of the central air-conditioning refrigeration unit will be greatly improved. The capacity of related equipment components is greatly reduced, the initial investment and operating costs are greatly reduced, and the dry operation of the indoor fan coil unit can be realized, which completely solves the indoor air pollution caused by the large number of harmful microorganisms in the water receiving pan of the air pan. Pollution and air conditioning disease.
同时,若在冬季条件下的空调设计、运行中直接采用这一方式实现加湿热回收过程,则可省去了另设的加湿器,此时的加湿水源主要为软化水。At the same time, if this method is directly used in the design and operation of the air conditioner in winter to realize the heat recovery process of humidification, an additional humidifier can be omitted, and the humidification water source at this time is mainly softened water.
本实用新型在结构形式及尺寸、运行调节的可控性及可靠性、能效比与经济性方面,比现有形式的新排风热回收器具有很大的综合优势,例如其冬季的能效比可真正达到6~8以上,且可有效避免结露结冰等限制问题。Compared with the existing new exhaust heat recovery device, the utility model has great comprehensive advantages in terms of structural form and size, controllability and reliability of operation adjustment, energy efficiency ratio and economy, such as its energy efficiency ratio in winter It can really reach more than 6-8, and can effectively avoid restrictive problems such as condensation and icing.
本实用新型实现了制冷机组冷凝换热原理和应用两个方面的重大突破。The utility model realizes a major breakthrough in two aspects of the refrigeration unit condensation heat exchange principle and application.
附图说明 Description of drawings
图1分别是本实用新型原理示意图。Fig. 1 is respectively the principle schematic diagram of the utility model.
图1中各部件编号与名称如下:The numbers and names of the parts in Figure 1 are as follows:
压缩机1、四通阀2、室外翅片式加湿冷却冷凝器3、单向阀组4+5+6+7、储液器8、干燥过滤器9、视液镜10、膨胀阀11、蒸发器12、汽液分离器13、低压表14、高压表15、蒸发器接水盘16、一级冷凝加热器17、二级加湿冷却器18、三级冷凝加热器19、二级加湿冷却器加湿水盘20、加湿器喷口21。Compressor 1, four-
具体实施方式 Detailed ways
下面结合附图和一种具体的实施应用例对本实用新型做进一步的说明。The utility model will be further described below in conjunction with the accompanying drawings and a specific implementation and application example.
图1是本实用新型原理示意图。Fig. 1 is a schematic diagram of the principle of the utility model.
该实用新型由压缩机(1)、室外翅片式加湿冷却冷凝器(3)、蒸发器(12)、膨胀阀(11)、四通阀(2)、单向阀组(4、5、6、7)、储液器(8)、干燥过滤器(9)、汽液分离器(13)及其它配件组成,其特征在于室外翅片式加湿冷却冷凝器(3)由一级冷凝加热器(17)、二级加湿冷却器(18)、三级冷凝加热器(19)等多级热湿处理组件组成;室外翅片式加湿冷却冷凝器(3)氟路进口端经四通阀(2)与压缩机(1)排气口相连,出口端与单向阀组(4+5+6+7)相连;储液器(8)进口端与单向阀组(4+5+6+7)相连,出口端与干燥过滤器(9)进口相连;干燥过滤器(9)出口端经视液镜(10)与膨胀阀(11)进口相连;蒸发器(12)进口端通过单向阀组(4+5+6+7)与膨胀阀(11)出口相连,出口端通过四通阀(2)与汽液分离器(13)进口端相连;汽液分离器(13)出口端与压缩机(1)吸气口相连。The utility model consists of a compressor (1), an outdoor finned humidification cooling condenser (3), an evaporator (12), an expansion valve (11), a four-way valve (2), a one-way valve group (4, 5, 6, 7), liquid receiver (8), dry filter (9), vapor-liquid separator (13) and other accessories, characterized in that the outdoor finned humidification and cooling condenser (3) is heated by one-stage condensation (17), two-stage humidification cooler (18), three-stage condensing heater (19) and other multi-stage heat and humidity treatment components; the outdoor finned humidification cooling condenser (3) fluorine circuit inlet end passes through a four-way valve (2) Connected to the exhaust port of the compressor (1), the outlet port is connected to the one-way valve group (4+5+6+7); the inlet port of the liquid reservoir (8) is connected to the one-way valve group (4+5+ 6+7), the outlet end is connected to the inlet of the drier filter (9); the outlet end of the drier filter (9) is connected to the inlet of the expansion valve (11) through the sight glass (10); the inlet end of the evaporator (12) passes through The one-way valve group (4+5+6+7) is connected to the outlet of the expansion valve (11), and the outlet is connected to the inlet of the vapor-liquid separator (13) through the four-way valve (2); the vapor-liquid separator (13) The outlet end is connected with the suction port of the compressor (1).
室外翅片式加湿冷却冷凝器(3)二级加湿冷却装置(18)的加湿水盘(20)的进水口与蒸发器(12)接水盘(16)出水管与相连,出水口与加湿器喷口(21)相连。二级加湿冷却器(18)进风端与一级冷凝加热器(17)出风端相连,出风端与三级冷凝加热器(19)相连。蒸发器(12)位于冷凝器(2)上部,蒸发器冷凝水通过水管输送到二级加湿冷却器加湿水盘(20)并用超声波加湿喷嘴(21)对空气加湿冷却。The water inlet of the humidification water pan (20) of the outdoor finned humidification cooling condenser (3) secondary humidification cooling device (18) is connected with the water outlet pipe of the evaporator (12) water receiving pan (16), and the water outlet is connected with the humidification The device nozzle (21) is connected. The air inlet end of the secondary humidification cooler (18) is connected with the air outlet end of the first-stage condensation heater (17), and the air outlet end is connected with the third-stage condensation heater (19). The evaporator (12) is located on the upper part of the condenser (2), and the condensed water of the evaporator is transported to the humidification water pan (20) of the secondary humidification cooler through water pipes, and the air is humidified and cooled by the ultrasonic humidification nozzle (21).
按照上述结构制作而成的空气源热泵机组,在冷凝器一侧可先利用冷却空气的显冷量对冷凝器内高温高压的制冷机进行冷却,当空气达到较高温度时,就采用喷水的方式进行加湿降温,空气中含湿量大为增加,而沿近似等焓线降温,然后与制冷剂进行二次冷却换热,从而实现了在大大减少冷却风量的情况下进行冷凝换热,且冷凝温度大大低于常规风冷热泵,从而大大改善了冷凝状况,热泵能效比大为提高,同时避免了水冷热泵必须另建冷却塔进行冷却,节约了初投资和运行费用。The air source heat pump unit manufactured according to the above structure can first use the sensible cooling capacity of the cooling air to cool the high temperature and high pressure refrigerator in the condenser on the side of the condenser. When the air reaches a higher temperature, spray water Humidification and cooling are carried out in the way of humidification, the moisture content in the air is greatly increased, and the temperature is lowered along the approximate isenthalpy line, and then the secondary cooling and heat exchange with the refrigerant is carried out, thereby realizing the condensation heat exchange under the condition of greatly reducing the cooling air volume, And the condensing temperature is much lower than that of conventional air-cooled heat pumps, which greatly improves the condensation situation and the energy efficiency ratio of heat pumps. At the same time, it avoids the need to build a cooling tower for cooling water-cooled heat pumps, saving initial investment and operating costs.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101799192A (en) * | 2010-03-25 | 2010-08-11 | 北京水木泽清能源科技有限公司 | Water source heat pump concentrated air conditioner for ship |
CN101435651B (en) * | 2008-12-11 | 2011-04-20 | 广州东誉工业设备有限公司 | Mute energy-saving freezing type drier |
CN102213465A (en) * | 2010-04-07 | 2011-10-12 | 北京水木泽清能源科技有限公司 | Temperature-humidity separately-controlled central air conditioner of water source heat pump for ship |
CN104819591A (en) * | 2015-04-24 | 2015-08-05 | 河南佰衡节能技术有限公司 | Agricultural local product heating pump drying device with refrigeration function |
CN105637302A (en) * | 2013-10-01 | 2016-06-01 | 株式会社德山科特兰 | Thermo-hygrostat using compressor discharged heat source |
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2007
- 2007-12-13 CN CN200720310534.XU patent/CN201138102Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101435651B (en) * | 2008-12-11 | 2011-04-20 | 广州东誉工业设备有限公司 | Mute energy-saving freezing type drier |
CN101799192A (en) * | 2010-03-25 | 2010-08-11 | 北京水木泽清能源科技有限公司 | Water source heat pump concentrated air conditioner for ship |
CN102213465A (en) * | 2010-04-07 | 2011-10-12 | 北京水木泽清能源科技有限公司 | Temperature-humidity separately-controlled central air conditioner of water source heat pump for ship |
CN105637302A (en) * | 2013-10-01 | 2016-06-01 | 株式会社德山科特兰 | Thermo-hygrostat using compressor discharged heat source |
CN104819591A (en) * | 2015-04-24 | 2015-08-05 | 河南佰衡节能技术有限公司 | Agricultural local product heating pump drying device with refrigeration function |
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