CN103743151A - Automobile waste heat recovering parking air-conditioner based on absorption type refrigerating and working method thereof - Google Patents
Automobile waste heat recovering parking air-conditioner based on absorption type refrigerating and working method thereof Download PDFInfo
- Publication number
- CN103743151A CN103743151A CN201310675642.7A CN201310675642A CN103743151A CN 103743151 A CN103743151 A CN 103743151A CN 201310675642 A CN201310675642 A CN 201310675642A CN 103743151 A CN103743151 A CN 103743151A
- Authority
- CN
- China
- Prior art keywords
- cold
- heat
- automobile
- solid
- chemical reaction
- 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
- 239000002918 waste heat Substances 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000010521 absorption reaction Methods 0.000 title claims 8
- 239000007789 gas Substances 0.000 claims abstract description 81
- 239000003507 refrigerant Substances 0.000 claims abstract description 81
- 238000006243 chemical reaction Methods 0.000 claims abstract description 68
- 238000005057 refrigeration Methods 0.000 claims abstract description 39
- 239000012782 phase change material Substances 0.000 claims abstract description 34
- 239000003463 adsorbent Substances 0.000 claims abstract description 32
- 239000000126 substance Substances 0.000 claims abstract description 29
- 238000004378 air conditioning Methods 0.000 claims abstract description 9
- 238000004146 energy storage Methods 0.000 claims description 23
- 239000007787 solid Substances 0.000 claims description 20
- 239000013529 heat transfer fluid Substances 0.000 claims description 17
- 230000008569 process Effects 0.000 claims description 12
- 238000003795 desorption Methods 0.000 claims description 7
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 230000009466 transformation Effects 0.000 claims 2
- 230000015556 catabolic process Effects 0.000 claims 1
- 239000012530 fluid Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 103
- 238000001816 cooling Methods 0.000 abstract description 44
- 239000007788 liquid Substances 0.000 abstract description 36
- 238000011084 recovery Methods 0.000 abstract description 10
- 230000007175 bidirectional communication Effects 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 description 44
- 238000005516 engineering process Methods 0.000 description 6
- 238000005338 heat storage Methods 0.000 description 6
- 238000005381 potential energy Methods 0.000 description 6
- 230000008901 benefit Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 230000002457 bidirectional effect Effects 0.000 description 2
- 238000002144 chemical decomposition reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000013332 literature search Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
Images
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
Landscapes
- Sorption Type Refrigeration Machines (AREA)
- Air-Conditioning For Vehicles (AREA)
Abstract
本发明提供了一种基于吸附式制冷的汽车废热回收停车空调,固气化学反应吸附床内设有化学吸附剂,吸附床换热盘管设置于固气化学反应吸附床内,吸附床换热盘管的入口端收集汽车尾气热量,吸附床换热盘管的出口端与汽车废气排气管相连;固气化学反应吸附床通过管路III与制冷剂储液器双向连通;相变材料存储器及换热管盘设置于制冷剂储液器内,相变材料存储器及换热管盘的出口端和入口端分别与汽车厢体相连通;同时提供其工作方法。在车辆行驶条件下,利用汽车废气热量通过吸附式制冷循环产生冷量存储于相变材料中。在停车状态下工作,不消耗车内原有能源,利用存储于相变材料中的制冷冷量进行制冷空调工作,调节车内温度在舒适范围之内。
The invention provides a car waste heat recovery parking air conditioner based on adsorption refrigeration. A chemical adsorbent is arranged in a solid-gas chemical reaction adsorption bed, and a heat exchange coil of the adsorption bed is arranged in the solid-gas chemical reaction adsorption bed. The inlet end of the coil collects the heat of automobile exhaust, and the outlet end of the heat exchange coil of the adsorption bed is connected to the exhaust pipe of the automobile; the solid-gas chemical reaction adsorption bed is in bidirectional communication with the refrigerant liquid receiver through pipeline III; the phase change material storage and the heat exchange tube coil are arranged in the refrigerant liquid storage, and the outlet end and the inlet port of the phase change material storage and the heat exchange tube coil are respectively connected with the car body; meanwhile, the working method thereof is provided. Under the driving condition of the vehicle, the heat of the exhaust gas of the vehicle is used to generate cold energy through the adsorption refrigeration cycle and store it in the phase change material. Working in the parking state, without consuming the original energy in the car, the cooling capacity stored in the phase change material is used for refrigeration and air conditioning, and the temperature in the car is adjusted within the comfortable range.
Description
技术领域technical field
本发明涉及吸附式制冷利用技术领域的装置,具体是一种基于吸附式制冷的汽车废热回收停车空调及其工作方法。The invention relates to a device in the technical field of adsorption refrigeration utilization, in particular to an adsorption refrigeration-based automobile waste heat recovery parking air conditioner and a working method thereof.
背景技术Background technique
随着人民生活水平提高,汽车已逐渐成为生活必需品,人们对汽车舒适性要求也有相应的大幅度提高,舒适节能的空调系统是其中的重要要求之一。With the improvement of people's living standards, cars have gradually become necessities of life, and people's requirements for car comfort have also been greatly improved. Comfortable and energy-saving air-conditioning systems are one of the important requirements.
当前的汽车空调主要采用压缩机制冷,其能源来自内燃机的驱动,消耗额外的能源;同时制冷剂在多年的技术更新和改良后,仍无法保证其制冷剂对臭氧层无破坏作用。在节能和环保两方面都有较大的缺点。The current automobile air conditioner mainly adopts compressor refrigeration, and its energy comes from the drive of internal combustion engine, which consumes extra energy. At the same time, after years of technological updates and improvements, the refrigerant still cannot guarantee that its refrigerant will not damage the ozone layer. Both energy saving and environmental protection have relatively large disadvantages.
吸附制冷具有零ODP,零GWP的特点,能够利用低品位热源的优点,是一项新世纪蓬勃发展的制冷方式。虽然在技术上还不成熟,但已走出实验室,成为实际利用意义较大的一种制冷技术。目前汽车空调采用蒸汽压缩式制冷系统,利用发动机轴功率驱动,提供舒适空调,其代价是增加了能源消耗,增加空气污染,而吸附式制冷汽车空调,其热源主要是发动机的余热,包括汽车冷却水废热以及汽车尾气废热,是一个可以加以利用巨大资源。目前驱动汽车、火车、船舶等运输工具的制冷设备都需要消耗额外的燃料,而这些运输工具的发动机排气、发动机冷却介质能产生大量余热。吸附制冷系统利用余热驱动,无须额外能源,结构简单,抗震性能好,特别适宜于汽车、火车、船舶等运输工具内的制冷。Adsorption refrigeration has the characteristics of zero ODP and zero GWP, and can take advantage of the advantages of low-grade heat sources. It is a vigorously developing refrigeration method in the new century. Although it is not yet mature in technology, it has already stepped out of the laboratory and become a refrigeration technology with great practical significance. At present, the automobile air conditioner adopts the vapor compression refrigeration system, which is driven by the shaft power of the engine to provide comfortable air conditioning. The cost is to increase energy consumption and increase air pollution. However, the heat source of the adsorption refrigeration automobile air conditioner is mainly the waste heat of the engine, including automobile cooling. Water waste heat, as well as vehicle exhaust waste heat, is a huge resource that can be utilized. At present, the refrigeration equipment that drives vehicles, trains, ships and other means of transportation needs to consume additional fuel, and the engine exhaust and engine cooling medium of these means of transportation can generate a lot of waste heat. The adsorption refrigeration system is driven by waste heat, does not require additional energy, has a simple structure and good shock resistance, and is especially suitable for refrigeration in transportation vehicles such as automobiles, trains, and ships.
然而汽车废热是一种随时间而变化的低密度能源,具有间歇性、不稳定性的特点,为了实现吸附式停车空调的广泛应用,在提高能量回收利用效率,实施汽车废热的高效能量储存技术是解决其间歇性、不稳定性及能量供需时间差矛盾的必须手段。目前,热能储存方法主要有显热储能和潜热储能两种形式,其中显热储能技术简单、运行管理方便,但储能密度较低致使贮热装置体积庞大,另外,采用显热式储能装置在能量释放过程中存在输出温度波动大的缺点。潜热储能采用相变材料实现能量储存,其储能密度较高,且储热、释热过程近似等温,易于系统运行匹配,可进行制冷冷量的储存。However, automobile waste heat is a low-density energy that changes with time, and has the characteristics of intermittent and unstable. In order to realize the wide application of adsorption parking air conditioners, the efficient energy storage technology of automobile waste heat is implemented to improve the efficiency of energy recovery and utilization. It is a necessary means to solve the contradiction between intermittent, unstable and energy supply and demand time difference. At present, thermal energy storage methods mainly include sensible heat storage and latent heat storage. Among them, the sensible heat storage technology is simple and easy to operate and manage, but the low energy storage density makes the heat storage device bulky. In addition, the sensible heat storage method is adopted The energy storage device has the disadvantage of large output temperature fluctuations during the energy release process. Latent heat energy storage uses phase change materials to realize energy storage. Its energy storage density is high, and the heat storage and heat release processes are approximately isothermal, which is easy to match the system operation and can store refrigeration and cooling capacity.
特别是在夏日较长时间室外停车后,车内温度较高,在现有车载空调条件下,所需制冷时间较长,能源消耗较大,且严重影响用户舒适度体验。以上问题,现有国内外资料均未提出解决方案。Especially after a long period of outdoor parking in summer, the temperature inside the car is high. Under the existing vehicle air conditioner conditions, the required cooling time is longer, the energy consumption is larger, and the user's comfort experience is seriously affected. The above problems, the existing domestic and foreign data all do not propose a solution.
经对现有技术的文献检索,目前尚无利用化学吸附技术利用汽车废热进行制冷并将制冷冷量储存的停车空调装置的专利。According to literature search of the prior art, there is no patent for a parking air-conditioning device that utilizes the waste heat of automobiles to refrigerate and stores the refrigerated cooling capacity by using chemical adsorption technology.
发明内容Contents of the invention
本发明针对现有技术中存在的上述不足,提供了一种基于吸附式制冷的汽车废热回收停车空调及其工作方法,该空调以硅胶-水工质对吸附制冷,可以在不依赖汽车内部原有的能源系统情况下,通过利用车辆运行时的废热进行制冷工作和制冷系统控制,并将制冷冷量加以存储,在太阳照射的停车场合,保持车内温度在舒适范围内,同时,不需要汽车启动后启动原有空调系统进行散热,达到了提高用户舒适度体验和节约能源的目的。Aiming at the above-mentioned deficiencies in the prior art, the present invention provides a car waste heat recovery parking air conditioner based on adsorption refrigeration and its working method. In the case of some energy systems, by using the waste heat when the vehicle is running to perform refrigeration work and refrigeration system control, and store the cooling capacity, the temperature in the car can be kept within a comfortable range when the car is parked in the sun. At the same time, no After the car is started, the original air conditioning system is activated for heat dissipation, which achieves the purpose of improving user comfort experience and saving energy.
本发明是通过以下技术方案实现的。The present invention is achieved through the following technical solutions.
根据本发明的一个方面,提供了一种基于吸附式制冷的汽车废热回收停车空调,包括固气化学反应吸附床、吸附床换热盘管、制冷剂储液器以及相变材料存储器及换热管盘,其中,所述固气化学反应吸附床的内部设置有化学吸附剂,所述吸附床换热盘管设置于固气化学反应吸附床的内部,吸附床换热盘管的入口端通过管路I收集汽车尾气热量,吸附床换热盘管的出口端通过管路II与汽车废气排气管相连,构成空调传热流体流动环路;所述固气化学反应吸附床通过管路III与制冷剂储液器双向连通,构成了制冷剂双向流动环路,从而将固气化学反应吸附床内解吸出的制冷剂在固气化学反应吸附床和制冷剂储液器之间双向流动;所述相变材料存储器及换热管盘设置于制冷剂储液器的内部,相变材料存储器及换热管盘的出口端和入口端分别通过管路IV和管路V与汽车厢体相连通,构成了冷用户端传热流体流动环路。According to one aspect of the present invention, a car waste heat recovery parking air conditioner based on adsorption refrigeration is provided, including a solid-gas chemical reaction adsorption bed, an adsorption bed heat exchange coil, a refrigerant liquid reservoir, a phase change material storage and a heat exchange The tube tray, wherein, the inside of the solid-gas chemical reaction adsorption bed is provided with chemical adsorbent, the heat exchange coil of the adsorption bed is arranged inside the solid-gas chemical reaction adsorption bed, and the inlet end of the adsorption bed heat exchange coil passes through Pipeline I collects the heat of automobile exhaust, and the outlet end of the heat exchange coil of the adsorption bed is connected to the exhaust pipe of the automobile through pipeline II to form a flow loop of the air-conditioning heat transfer fluid; the solid-gas chemical reaction adsorption bed passes through pipeline III Two-way communication with the refrigerant liquid receiver constitutes a refrigerant two-way flow loop, so that the refrigerant desorbed in the solid-gas chemical reaction adsorption bed flows in both directions between the solid-gas chemical reaction adsorption bed and the refrigerant liquid receiver; The phase change material storage and the heat exchange tube coil are arranged inside the refrigerant liquid receiver, and the outlet end and the inlet end of the phase change material storage and the heat exchange tube coil are respectively connected to the car body through the pipeline IV and the pipeline V The flow loop of the heat transfer fluid at the cold user end is formed.
优选地,所述管路I位于固气化学反应吸附床的外部,管路I上设有汽车尾气调节阀。Preferably, the pipeline I is located outside the solid-gas chemical reaction adsorption bed, and the pipeline I is provided with an automobile exhaust regulating valve.
优选地,所述管路III上设有制冷剂调节阀。Preferably, the pipeline III is provided with a refrigerant regulating valve.
优选地,所述管路IV位于制冷剂储液器的外部,管路IV上设有冷量调节阀。Preferably, the pipeline IV is located outside the refrigerant accumulator, and the pipeline IV is provided with a cooling capacity regulating valve.
优选地,所述管路V位于制冷剂储液器的外部,管路V上设有空气流动循环泵。Preferably, the pipeline V is located outside the refrigerant accumulator, and the pipeline V is provided with an air circulation pump.
优选地,所述基于吸附式制冷的汽车废热回收停车空调,还包括尾气集热器,所述尾气集热器连接于管路I的入口端。Preferably, the adsorption-type refrigeration-based automobile waste heat recovery parking air conditioner also includes an exhaust gas collector connected to the inlet end of the pipeline I.
根据本发明的另一个方面,提供了上述基于吸附式制冷的汽车废热回收停车空调的工作方法,包括以下三个阶段:According to another aspect of the present invention, there is provided the above-mentioned working method of the above-mentioned adsorption refrigeration-based automobile waste heat recovery parking air conditioner, which includes the following three stages:
第一阶段,汽车废气热能储能阶段:汽车运行过程中,利用空调传热流体流动环路所获得的热量为固气化学反应吸附床内的化学吸附剂提供解吸热,使化学吸附剂发生化学分解反应,实现尾气热能向化学吸附势能的转化储存,解吸出的制冷剂蒸汽进入制冷剂储液器凝结成液体储存起来,从而实现对汽车废气热能的转化储存;The first stage, the thermal energy storage stage of automobile exhaust gas: during the operation of the automobile, the heat obtained by the flow loop of the heat transfer fluid of the air conditioner is used to provide the desorption heat for the chemical adsorbent in the solid-gas chemical reaction adsorption bed, so that the chemical adsorbent The chemical decomposition reaction realizes the conversion and storage of exhaust gas heat energy to chemical adsorption potential energy, and the desorbed refrigerant vapor enters the refrigerant liquid receiver to condense into a liquid for storage, thereby realizing the conversion and storage of automobile exhaust gas heat energy;
第二阶段,汽车制冷冷量储存阶段:汽车尾气调节阀关闭,固气化学反应吸附床温度下降,固气化学反应吸附床内化学吸附剂与制冷剂储液器内的制冷剂发生化学合成反应,利用制冷剂储液器内的制冷剂在低温低压下发生蒸发向外界吸热,通过相变材料存储器及换热管盘将制冷冷量存储在相变材料中,从而实现对冷用户端制冷冷量的储存;The second stage, the storage stage of automobile refrigeration cold capacity: the automobile tail gas regulating valve is closed, the temperature of the solid-gas chemical reaction adsorption bed drops, and the chemical synthesis reaction occurs between the chemical adsorbent in the solid-gas chemical reaction adsorption bed and the refrigerant in the refrigerant liquid receiver , using the refrigerant in the refrigerant liquid receiver to evaporate at low temperature and low pressure to absorb heat from the outside, and store the cooling capacity in the phase change material through the phase change material storage and heat exchange tube disk, so as to realize the cooling of the cold user end cold storage;
第三个阶段,制冷冷量释放阶段:汽车停止工作后,冷量调节阀开启,将制冷冷量释放,从而实现对汽车停车状态下的制冷。The third stage, cooling capacity release stage: After the car stops working, the cooling capacity regulating valve opens to release the cooling capacity, thereby realizing the cooling when the car is parked.
与现有技术相比,本发明具有以下技术特点:Compared with the prior art, the present invention has the following technical characteristics:
第一,能量储存密度高:相对于传统的显热式和潜热式储能装置,本发明利用化学吸附势能实现能量的转化储存,其能量储存密度高,从而可减少设备体积,降低储能成本;First, high energy storage density: Compared with traditional sensible heat and latent heat energy storage devices, the present invention uses chemical adsorption potential energy to realize energy conversion and storage, and its energy storage density is high, thereby reducing equipment volume and energy storage costs ;
第二,储存能量损失小,易于长期储存:传统储能装置由于与外界环境有较大温差因而在能量储存过程中有较大的能量损失,而本发明采用热化学吸附储能技术,只要制冷剂与化学吸附储能材料相隔离不发生化学反应,能量就会一直储存并且不需要消耗能量去维持,因而便于长期储存;Second, the storage energy loss is small, and it is easy to store for a long time: the traditional energy storage device has a large temperature difference with the external environment, so there is a large energy loss in the energy storage process, while the present invention adopts thermochemical adsorption energy storage technology, as long as refrigeration The agent is separated from the chemical adsorption energy storage material without chemical reaction, the energy will be stored all the time and does not need to consume energy to maintain, so it is convenient for long-term storage;
第三,释能过程温度波动小:由于固气化学反应的单变量特性,在汽车尾气热能和制冷冷量释放阶段,能量输出温度波动小,近似为等温过程,易于系统运行匹配;Third, the temperature fluctuation during the energy release process is small: due to the univariate characteristics of the solid-gas chemical reaction, during the release stage of the heat energy and cooling capacity of the automobile exhaust, the energy output temperature fluctuation is small, which is approximately an isothermal process, and it is easy to match the system operation;
第四,整个系统除吸附床之外采用吸附制冷工作台所用标准件制成,设计要求较简化,同时有利于批量生产和市场推广。Fourth, the entire system is made of standard components used in adsorption refrigeration workbenches except for the adsorption bed. The design requirements are relatively simplified, and it is also conducive to mass production and market promotion.
附图说明Description of drawings
通过阅读参照以下附图对非限制性实施例所作的详细描述,本发明的其它特征、目的和优点将会变得更明显:Other characteristics, objects and advantages of the present invention will become more apparent by reading the detailed description of non-limiting embodiments made with reference to the following drawings:
图1为本发明结构示意图;Fig. 1 is a structural representation of the present invention;
图2为本发明热力学循环图;Fig. 2 is a thermodynamic cycle diagram of the present invention;
图中:1为汽车尾气调节阀,2为固气化学反应吸附床,3为制冷剂调节阀,4为吸附床换热盘管,5为化学吸附剂,6为制冷剂储液器,7为制冷剂,8为相变材料存储器及换热管盘,9为冷量调节阀,10为汽车厢体,11为空气流动循环泵。In the figure: 1 is the automobile exhaust regulating valve, 2 is the solid-gas chemical reaction adsorption bed, 3 is the refrigerant regulating valve, 4 is the heat exchange coil of the adsorption bed, 5 is the chemical adsorbent, 6 is the refrigerant liquid receiver, 7 Refrigerant, 8 is a phase change material storage and heat exchange tube coil, 9 is a cooling capacity regulating valve, 10 is a car body, and 11 is an air flow circulation pump.
具体实施方式Detailed ways
下面对本发明的实施例作详细说明:本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程。应当指出的是,对本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。The following is a detailed description of the embodiments of the present invention: this embodiment is implemented on the premise of the technical solution of the present invention, and provides detailed implementation methods and specific operation processes. It should be noted that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention, and these all belong to the protection scope of the present invention.
如图1所示,本实施例提供了一种基于吸附式制冷的汽车废热回收停车空调,包括固气化学反应吸附床、吸附床换热盘管、制冷剂储液器以及相变材料存储器及换热管盘,其中,所述固气化学反应吸附床的内部设置有化学吸附剂,所述吸附床换热盘管设置于固气化学反应吸附床的内部,吸附床换热盘管的入口端通过管路I采集汽车尾气,吸附床换热盘管的出口端通过管路II与汽车废气排气管相连;所述固气化学反应吸附床通过管路III与制冷剂储液器双向连通;所述相变材料存储器及换热管盘设置于制冷剂储液器的内部,相变材料存储器及换热管盘的出口端和入口端分别通过管路IV和管路V与汽车厢体相连通;As shown in Figure 1, this embodiment provides a car waste heat recovery parking air conditioner based on adsorption refrigeration, including a solid-gas chemical reaction adsorption bed, an adsorption bed heat exchange coil, a refrigerant liquid storage device, and a phase change material storage device. The heat exchange tube coil, wherein, the interior of the solid-gas chemical reaction adsorption bed is provided with a chemical adsorbent, the adsorption bed heat exchange coil is arranged inside the solid-gas chemical reaction adsorption bed, and the inlet of the adsorption bed heat exchange coil The exhaust gas of the automobile is collected through the pipeline I, and the outlet end of the heat exchange coil of the adsorption bed is connected with the exhaust pipe of the automobile through the pipeline II; the solid-gas chemical reaction adsorption bed is bidirectionally connected with the refrigerant liquid receiver through the pipeline III The phase-change material storage and the heat exchange tube coil are arranged inside the refrigerant liquid receiver, and the outlet end and the inlet port of the phase change material storage and the heat exchange tube coil are respectively connected to the car body through the pipeline IV and the pipeline V. Connected;
所述管路I的出口与吸附床换热盘管的进口相连,吸附床换热盘管的出口通过管路II与汽车废气排气管相连,从而构成空调传热流体流动环路;所述相变材料存储器及换热管盘、管路IV、汽车厢体、管路V和相变材料存储器及换热管盘依次相连,构成了冷用户端传热流体流动环路;所述固气化学反应吸附床、管路III和制冷剂储液器依次相连,构成了制冷剂双向流动环路,从而将固气化学反应吸附床内解吸出的制冷剂在固气化学反应吸附床和制冷剂储液器之间双向流动。The outlet of the pipeline I is connected to the inlet of the heat exchange coil of the adsorption bed, and the outlet of the heat exchange coil of the adsorption bed is connected to the exhaust pipe of the automobile through the pipeline II, thereby forming an air-conditioning heat transfer fluid flow loop; The phase change material storage and the heat exchange tube disk, the pipeline IV, the car body, the pipeline V and the phase change material storage and the heat exchange tube disk are connected in sequence to form a cold user end heat transfer fluid flow loop; the solid gas The chemical reaction adsorption bed, pipeline III and the refrigerant liquid receiver are connected in sequence to form a two-way refrigerant flow loop, so that the refrigerant desorbed in the solid-gas chemical reaction adsorption bed is transferred between the solid-gas chemical reaction adsorption bed and the refrigerant Bi-directional flow between reservoirs.
进一步地,所述管路I位于固气化学反应吸附床的外部,管路I上设有汽车尾气调节阀。Further, the pipeline I is located outside the solid-gas chemical reaction adsorption bed, and the pipeline I is provided with an automobile exhaust regulating valve.
进一步地,所述管路III上设有制冷剂调节阀。Further, the pipeline III is provided with a refrigerant regulating valve.
进一步地,所述管路IV位于制冷剂储液器的外部,管路IV上设有冷量调节阀。Further, the pipeline IV is located outside the refrigerant accumulator, and the pipeline IV is provided with a cooling capacity regulating valve.
进一步地,所述管路V位于制冷剂储液器的外部,管路V上设有空气流动循环泵。Further, the pipeline V is located outside the refrigerant accumulator, and the pipeline V is provided with an air circulation pump.
进一步地,还包括尾气集热器,所述尾气集热器连接于管路I的入口端。Further, a tail gas heat collector is also included, and the tail gas heat collector is connected to the inlet end of the pipeline I.
如图2所示,本实施例提供的基于吸附式制冷的汽车废热回收停车空调,其工作方法包括以下三个阶段:As shown in Fig. 2, the car waste heat recovery parking air conditioner based on adsorption refrigeration provided in this embodiment, its working method includes the following three stages:
第一阶段,汽车废气热能储能阶段:汽车运行过程中,利用空调传热流体流动环路所获得的热量为固气化学反应吸附床内的化学吸附剂提供解吸热,使化学吸附剂发生化学分解反应,实现尾气热能向化学吸附势能的转化储存,解吸出的制冷剂蒸汽进入制冷剂储液器凝结成液体储存起来,从而实现对汽车废气热能的转化储存;The first stage, the thermal energy storage stage of automobile exhaust gas: during the operation of the automobile, the heat obtained by the flow loop of the heat transfer fluid of the air conditioner is used to provide the desorption heat for the chemical adsorbent in the solid-gas chemical reaction adsorption bed, so that the chemical adsorbent The chemical decomposition reaction realizes the conversion and storage of exhaust gas heat energy to chemical adsorption potential energy, and the desorbed refrigerant vapor enters the refrigerant liquid receiver to condense into a liquid for storage, thereby realizing the conversion and storage of automobile exhaust gas heat energy;
第二阶段,汽车制冷冷量储存阶段:汽车尾气调节阀关闭,固气化学反应吸附床温度下降,固气化学反应吸附床内化学吸附剂与制冷剂储液器内的制冷剂发生化学合成反应,利用制冷剂储液器内的制冷剂在低温低压下发生蒸发向外界吸热,通过相变材料存储器及换热管盘将制冷冷量存储在相变材料中,从而实现对冷用户端制冷冷量的储存;The second stage, the storage stage of automobile refrigeration cold capacity: the automobile tail gas regulating valve is closed, the temperature of the solid-gas chemical reaction adsorption bed drops, and the chemical synthesis reaction occurs between the chemical adsorbent in the solid-gas chemical reaction adsorption bed and the refrigerant in the refrigerant liquid receiver , using the refrigerant in the refrigerant liquid receiver to evaporate at low temperature and low pressure to absorb heat from the outside, and store the cooling capacity in the phase change material through the phase change material storage and heat exchange tube disk, so as to realize the cooling of the cold user end cold storage;
第三个阶段,制冷冷量释放阶段:汽车停止工作后,冷量调节阀开启,将制冷冷量释放,从而实现对汽车停车状态下的制冷。The third stage, cooling capacity release stage: After the car stops working, the cooling capacity regulating valve opens to release the cooling capacity, thereby realizing the cooling when the car is parked.
本实施例具体为:This embodiment is specifically:
本实施例提供的基于吸附式制冷的汽车废热回收停车空调,包括:汽车尾气调节阀1、固气化学反应吸附床2、制冷剂调节阀3、吸附床换热盘管4、化学吸附剂5、制冷剂储液器6、制冷剂7、相变材料存储器及换热管盘8、冷量调节阀9、汽车厢体10以及空气流动循环泵11。The car waste heat recovery parking air conditioner based on adsorption refrigeration provided in this embodiment includes: a car
其中:汽车尾气调节阀1的出口和吸附床换热盘管4的进口相连;吸附床换热盘管4的出口和汽车废气排气管相连;固气化学反应吸附床2的出口和制冷剂调节阀3的进口相连,制冷剂调节阀3的出口和制冷剂储液器6的进口相连,固气化学反应吸附床2内设有吸附床换热盘管4,化学吸附剂5填装于固气化学反应吸附床2内,制冷剂储液器6内设有相变材料存储器及换热管盘8,制冷剂7填装于制冷剂储液器6内;相变材料存储器及换热管盘8的出口与冷量调节阀9的入口相连,冷量调节阀9的出口与汽车厢体10的入口相连,汽车厢体10的出口与空气流动循环泵11相连。Among them: the outlet of the automobile
所述的制冷剂的流动方向是双向的,在汽车尾气加热吸附床阶段,制冷剂7依次流经固气化学反应吸附床2、制冷剂调节阀3和制冷剂储液器6;在吸附床降温阶段阶段,制冷剂7依次流经制冷剂储液器6、制冷剂调节阀3和固气化学反应吸附床2。The flow direction of the refrigerant is bi-directional. In the stage of heating the adsorption bed by the exhaust gas of the automobile, the
所述的汽车尾气调节阀1、固气化学反应吸附床2结合,构成固体化学反应吸附床的传热流体流动。The combination of the automobile tail
所述的制冷剂储液器6、相变材料存储器及换热管盘8、冷量调节阀9、汽车厢体10以及空气流动循环泵11依次相连,构成了制冷端的传热流体流动环路。The refrigerant
汽车废气热能储能阶段,能量由吸附床换热盘管向固体化学反应吸附床发生传递,通过汽车废气热能转化为化学吸附势能实现能量储存。In the stage of thermal energy storage of automobile exhaust gas, the energy is transferred from the heat exchange coil of the adsorption bed to the solid chemical reaction adsorption bed, and the energy storage is realized by converting the thermal energy of automobile exhaust gas into chemical adsorption potential energy.
汽车制冷冷量储存阶段,固气化学反应吸附床2内化学吸附剂5的吸附作用,使得制冷剂储液器6内的制冷剂7发生蒸发相变,能量由制冷剂储液器向相变材料存储器8发生并加以储存汽车废气制冷冷量释能阶段,相变材料存储器及换热管盘8经制冷端的传热流体流动环路传递实现制冷冷量释放。During the cold capacity storage stage of automobile refrigeration, the adsorption of the
本实施例工作过程包括:汽车废气热能储能阶段、汽车制冷冷量储存阶段和汽车废气制冷冷量释能阶段,其中:The working process of this embodiment includes: the stage of energy storage of automobile waste gas thermal energy, the stage of storage of automobile refrigeration and cold capacity, and the stage of energy release of automobile waste gas refrigeration and cold capacity, wherein:
第一个阶段,汽车废气热能储能阶段。开启汽车废气调节阀1,关闭冷量调节阀9,关闭制冷剂调节阀3;汽车废气为高温传热流体,输送到吸附床换热盘管4为固体化学反应吸附床2内的化学吸附材料5提供解吸热,当固体化学反应吸附床2内的化学吸附材料5的温度加热到解吸温度时,开启制冷剂调节阀3,从固体化学反应吸附床2解吸出的制冷剂7蒸汽经制冷剂调节阀3流入制冷剂储液器6内发生凝结,释放的凝结热通过汽车外流动空气外界排入外界环境介质(空气和水),凝结成液态的制冷剂7储存起来,从而实现汽车废气热能向化学吸附势能的转化储存。The first stage is the stage of automobile exhaust heat energy storage. Open the automobile exhaust
第二阶段,汽车制冷冷量储存阶段。汽车废气调节阀1关闭,固体化学反应吸附床2温度由于外界空气的冷却从而下降,固体化学反应吸附床2内化学吸附剂5与制冷剂储液器6内的制冷剂7发生化学合成反应,利用制冷剂储液器6内制冷剂7在低温低压下发生蒸发向外界吸热,通过交换热管将制冷量存储在相相变材料存储器及换热管盘8中,从而实现制冷冷量的储存。The second stage is the storage stage of automobile refrigeration capacity. The automobile exhaust
第三个阶段,制冷冷量释放阶段。在汽车停止工作后,汽车废气调节阀1关闭,冷量调节阀9打开,经空气流动循环泵11将制冷冷量释放到汽车厢体10,从而实现对汽车停车状态下的制冷。The third stage is the cooling capacity release stage. After the automobile stops working, the exhaust
如图2所示,Pcond是汽车废气废热热能储存/释放阶段的工作压力,Pev是制冷冷量释放阶段的工作压力,Ta是吸附剂吸附温度,Tg是吸附剂解吸温度。As shown in Fig. 2, P cond is the working pressure in the storage/release stage of waste heat and heat energy of automobile exhaust gas, P ev is the working pressure in the cooling capacity release stage, T a is the adsorption temperature of the adsorbent, and T g is the desorption temperature of the adsorbent.
本实例中,汽车尾气调节阀设置于管路I上,汽车尾气调节阀的出口和吸附床换热盘管的进口相连;吸附床换热盘管的出口通过管路II和汽车废气排气管相连;制冷剂调节阀设置于管路III上,固气化学反应吸附床的出口和制冷剂调节阀的进口相连,制冷剂调节阀的出口和制冷剂储液器的进口相连,固气化学反应吸附床内设有吸附床换热盘管,化学吸附剂填装于固气化学反应吸附床内,制冷剂储液器内设有相变材料存储器及换热管盘,制冷剂填装于制冷剂储液器内;冷量调节阀设置于管路IV上,空气流动循环泵设置于管路V上,相变材料存储器及换热管盘的出口与冷量调节阀的入口相连,冷量调节阀的出口与汽车厢体的入口相连,汽车厢体的出口与空气流动循环泵相连。In this example, the automobile exhaust regulating valve is arranged on the pipeline I, and the outlet of the automobile exhaust regulating valve is connected with the inlet of the heat exchange coil of the adsorption bed; the outlet of the heat exchange coil of the adsorption bed passes through the pipeline II and the exhaust pipe of the automobile connected; the refrigerant regulating valve is set on pipeline III, the outlet of the solid-gas chemical reaction adsorption bed is connected to the inlet of the refrigerant regulating valve, the outlet of the refrigerant regulating valve is connected to the inlet of the refrigerant liquid receiver, and the solid-gas chemical reaction The adsorption bed is equipped with an adsorption bed heat exchange coil, and the chemical adsorbent is filled in the solid-gas chemical reaction adsorption bed. The cooling capacity regulating valve is set on the pipeline IV, the air circulation pump is set on the pipeline V, the outlet of the phase change material storage and the heat exchange tube plate is connected with the inlet of the cooling capacity regulating valve, and the cooling capacity The outlet of the regulating valve is connected with the inlet of the car body, and the outlet of the car body is connected with the air circulation pump.
所述的汽车尾气调节阀的出口和吸附床换热盘管的进口相连;吸附床换热盘管的出口和汽车废气排气管相连,构成该装置传热流体流动环路。The outlet of the automobile tail gas regulating valve is connected to the inlet of the heat exchange coil of the adsorption bed; the outlet of the heat exchange coil of the adsorption bed is connected to the exhaust pipe of the automobile to form a heat transfer fluid flow loop of the device.
所述的相变材料存储器及换热管盘、冷用户端调节阀、冷用户端、低温传热流体循环泵和相变材料存储器及换热管盘依次相连,构成了冷用户端的传热流体流动环路。The phase change material storage and heat exchange tube disk, the cold user end regulating valve, the cold user end, the low temperature heat transfer fluid circulation pump, the phase change material storage and the heat exchange tube disk are connected in sequence to form the heat transfer fluid at the cold user end flow loop.
所述的制冷剂储液器、相变材料存储器及换热管盘、冷量调节阀、汽车厢体以及空气流动循环泵依次相连,构成了制冷端的传热流体流动环路。The refrigerant liquid storage, phase change material storage, heat exchange tube coil, cooling capacity regulating valve, car body and air circulation pump are connected in sequence to form a heat transfer fluid flow loop at the cooling end.
所述的固气化学反应吸附床、制冷剂调节阀和制冷剂储液器依次相连,构成了制冷剂双向流动的环路。The solid-gas chemical reaction adsorption bed, the refrigerant regulating valve and the refrigerant liquid receiver are connected in sequence to form a bidirectional flow loop of the refrigerant.
所述的制冷剂的流动方向是双向的,制冷剂在吸附床、制冷剂调节阀和制冷剂储液器中双向流动。The flow direction of the refrigerant is bidirectional, and the refrigerant flows bidirectionally in the adsorption bed, the refrigerant regulating valve and the refrigerant liquid receiver.
汽车废气热能储能阶段,热力循环过程为A-B-C,工作压力为Pcond,储存过程的冷凝温度为Tg,该阶段利用汽车废气废热获得的热量为固气化学反应器2内化学吸附剂5提供解吸热,实现汽车废气热能向化学吸附势能的转化储存;In the stage of thermal energy storage of automobile exhaust gas, the thermodynamic cycle process is ABC, the working pressure is P cond , and the condensation temperature in the storage process is T g . In this stage, the heat obtained by using the waste heat of automobile exhaust gas is provided for the
在制冷冷量释放时,热力循环过程为C-D-A,工作压力为Pev,释放过程的吸附温度为Ta,该阶段利用固体化学吸附床内化学吸附床2内吸附剂5的吸附作用,使得制冷剂储液器6内制冷剂7在低温低压下发生相变向外界吸热,并将热量存储于相变材料存储器及换热管盘8内。When the refrigeration capacity is released, the thermodynamic cycle process is CDA, the working pressure is P ev , and the adsorption temperature in the release process is T a . In this stage, the adsorption of the adsorbent 5 in the chemical adsorption bed 2 in the solid chemical adsorption bed is used to make the refrigeration The
以上对本发明的具体实施例进行了描述。需要理解的是,本发明并不局限于上述特定实施方式,本领域技术人员可以在权利要求的范围内做出各种变形或修改,这并不影响本发明的实质内容。Specific embodiments of the present invention have been described above. It should be understood that the present invention is not limited to the specific embodiments described above, and those skilled in the art may make various changes or modifications within the scope of the claims, which do not affect the essence of the present invention.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310675642.7A CN103743151B (en) | 2013-12-11 | 2013-12-11 | Automobile waste heat based on absorption type refrigerating reclaims parking air conditioner and method of work thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310675642.7A CN103743151B (en) | 2013-12-11 | 2013-12-11 | Automobile waste heat based on absorption type refrigerating reclaims parking air conditioner and method of work thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103743151A true CN103743151A (en) | 2014-04-23 |
CN103743151B CN103743151B (en) | 2016-02-10 |
Family
ID=50500198
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310675642.7A Expired - Fee Related CN103743151B (en) | 2013-12-11 | 2013-12-11 | Automobile waste heat based on absorption type refrigerating reclaims parking air conditioner and method of work thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103743151B (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104890474A (en) * | 2015-06-04 | 2015-09-09 | 广东美的制冷设备有限公司 | Vehicular air conditioner and vehicle |
CN106414123A (en) * | 2014-05-22 | 2017-02-15 | 济州大学校产学协力团 | Vehicle cooling device capable of instant cooling, vehicle comprising same, and instant cooling method for vehicle |
CN106482557A (en) * | 2016-09-14 | 2017-03-08 | 上海交通大学 | The heat chemistry absorption heat-pipe apparatus that a kind of utilization low grade heat energy drives |
CN106803609A (en) * | 2017-01-17 | 2017-06-06 | 宁波大学 | A kind of new-energy automobile power battery cooling system |
CN107062683A (en) * | 2017-03-27 | 2017-08-18 | 上海交通大学 | A kind of salty Composite Adsorptive Thermal Energy Storage type refrigeration system and its application |
CN108357332A (en) * | 2017-01-16 | 2018-08-03 | 丰田自动车株式会社 | Has the air conditioner for vehicles of adsorption type heat pump |
CN108495979A (en) * | 2016-01-04 | 2018-09-04 | 泰恩河畔纽卡斯尔大学 | Energy storage system |
CN114654967A (en) * | 2020-12-23 | 2022-06-24 | 长城汽车股份有限公司 | Air conditioning system and vehicle |
CN115962586A (en) * | 2022-12-20 | 2023-04-14 | 江苏容汇通用锂业股份有限公司 | Direct solar adsorption brine concentration refrigeration system and use method |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0190702A1 (en) * | 1985-02-04 | 1986-08-13 | Hitachi, Ltd. | Heat storing apparatus |
JPH0913960A (en) * | 1995-06-28 | 1997-01-14 | Nippondenso Co Ltd | Combined system for heating device and cooling device for catalyst |
JPH09170846A (en) * | 1995-12-20 | 1997-06-30 | Aqueous Res:Kk | On-vehicle chemical heat pump |
JP2007223570A (en) * | 2006-02-27 | 2007-09-06 | Toyota Motor Corp | Cooling system |
CN101793447A (en) * | 2010-03-25 | 2010-08-04 | 上海交通大学 | Cold-heat combined supply solar thermochemical adsorption composite energy storing device |
DE102011109584A1 (en) * | 2011-08-07 | 2013-02-07 | VauQuadrat GmbH | Air-conditioning device for motor car, has heat-driven refrigerating machine whose condensation temperature is high due to process condition such that condensation temperature is sufficient for re-cooling radiator of vehicle |
JP2013096586A (en) * | 2011-10-28 | 2013-05-20 | Sanden Corp | Adsorption type refrigeration device |
-
2013
- 2013-12-11 CN CN201310675642.7A patent/CN103743151B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0190702A1 (en) * | 1985-02-04 | 1986-08-13 | Hitachi, Ltd. | Heat storing apparatus |
JPH0913960A (en) * | 1995-06-28 | 1997-01-14 | Nippondenso Co Ltd | Combined system for heating device and cooling device for catalyst |
JPH09170846A (en) * | 1995-12-20 | 1997-06-30 | Aqueous Res:Kk | On-vehicle chemical heat pump |
JP2007223570A (en) * | 2006-02-27 | 2007-09-06 | Toyota Motor Corp | Cooling system |
CN101793447A (en) * | 2010-03-25 | 2010-08-04 | 上海交通大学 | Cold-heat combined supply solar thermochemical adsorption composite energy storing device |
DE102011109584A1 (en) * | 2011-08-07 | 2013-02-07 | VauQuadrat GmbH | Air-conditioning device for motor car, has heat-driven refrigerating machine whose condensation temperature is high due to process condition such that condensation temperature is sufficient for re-cooling radiator of vehicle |
JP2013096586A (en) * | 2011-10-28 | 2013-05-20 | Sanden Corp | Adsorption type refrigeration device |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106414123B (en) * | 2014-05-22 | 2019-03-15 | 济州大学校产学协力团 | Refrigeration device for vehicle capable of instant cooling, vehicle including the same, and instant cooling method for vehicle |
CN106414123A (en) * | 2014-05-22 | 2017-02-15 | 济州大学校产学协力团 | Vehicle cooling device capable of instant cooling, vehicle comprising same, and instant cooling method for vehicle |
CN104890474A (en) * | 2015-06-04 | 2015-09-09 | 广东美的制冷设备有限公司 | Vehicular air conditioner and vehicle |
CN108495979A (en) * | 2016-01-04 | 2018-09-04 | 泰恩河畔纽卡斯尔大学 | Energy storage system |
CN106482557A (en) * | 2016-09-14 | 2017-03-08 | 上海交通大学 | The heat chemistry absorption heat-pipe apparatus that a kind of utilization low grade heat energy drives |
CN106482557B (en) * | 2016-09-14 | 2019-04-19 | 上海交通大学 | A thermochemical adsorption heat pipe device driven by low-grade thermal energy |
CN108357332A (en) * | 2017-01-16 | 2018-08-03 | 丰田自动车株式会社 | Has the air conditioner for vehicles of adsorption type heat pump |
CN106803609A (en) * | 2017-01-17 | 2017-06-06 | 宁波大学 | A kind of new-energy automobile power battery cooling system |
CN107062683A (en) * | 2017-03-27 | 2017-08-18 | 上海交通大学 | A kind of salty Composite Adsorptive Thermal Energy Storage type refrigeration system and its application |
CN114654967A (en) * | 2020-12-23 | 2022-06-24 | 长城汽车股份有限公司 | Air conditioning system and vehicle |
CN114654967B (en) * | 2020-12-23 | 2024-05-17 | 长城汽车股份有限公司 | Air conditioning system and vehicle |
CN115962586A (en) * | 2022-12-20 | 2023-04-14 | 江苏容汇通用锂业股份有限公司 | Direct solar adsorption brine concentration refrigeration system and use method |
CN115962586B (en) * | 2022-12-20 | 2023-09-19 | 江苏容汇通用锂业股份有限公司 | A direct solar energy adsorption brine concentration refrigeration system and its use method |
Also Published As
Publication number | Publication date |
---|---|
CN103743151B (en) | 2016-02-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103743151B (en) | Automobile waste heat based on absorption type refrigerating reclaims parking air conditioner and method of work thereof | |
Choudhury et al. | An overview of developments in adsorption refrigeration systems towards a sustainable way of cooling | |
CN102155813B (en) | Thermochemical absorption and refrigeration device driven by condensation heat of air conditioning unit | |
CN101571330B (en) | A frost-free multifunctional solar-assisted heat pump system | |
CN102305494B (en) | An Absorption Chemical Energy Storage Device Containing Crystals | |
CN102787943A (en) | Engine waste heat recycling system utilizing organic working medium as cooling liquid | |
CN114877558B (en) | Solar-driven adsorption type cold-hot water cogeneration system for desert and method thereof | |
CN103912946A (en) | Mass recovery type adsorption refrigeration air-conditioning system on basis of phase-change heat storage | |
CN105522890B (en) | Automobile engine waste heat recycles air conditioning control device | |
CN106766356A (en) | A kind of solar energy assisted absorption refrigerating plant for refrigerator car | |
CN106114140A (en) | A kind of electric automobile heat of adsorption pond air conditioning system realizing cold and heat combined supply | |
CN100554824C (en) | Regenerative two-stage thermochemical adsorption refrigeration cycle system based on pressure swing desorption technology | |
CN106183719B (en) | A kind of system adjusting vehicle interior temperature using loop heat pipe | |
CN103884128B (en) | A kind of utilize automobile waste heat to drive absorption and compressed mixed refrigerated air-conditioning system | |
CN206171108U (en) | Engine waste heat recovery type vehicle -mounted air conditioning system | |
CN100575820C (en) | Multi-effect adsorption refrigeration cycle system | |
CN103940143A (en) | Solid adsorption air conditioner system driven by waste heat of automobile | |
CN203785313U (en) | Automobile waste heat-driven adsorption and compression hybrid refrigeration air conditioning system | |
CN211823259U (en) | Solar adsorption and absorption type combined indirect cooling system | |
CN109910544B (en) | Electric automobile thermal management system | |
CN101398238B (en) | Two-grade dual hot chemistry adsorption cooling cycle system | |
CN202547182U (en) | Device for converting heat energy of tail gas of automobile and ship to energy of air conditioners of automobile and ship | |
CN1967092A (en) | Refrigerating unit using waste heat from tail gas of internal combustion engine | |
CN204630145U (en) | A kind of absorption type air conditioner utilized based on residual heat of tail gas of automobile | |
CN103542602B (en) | Based on solar absorption refrigeration system and the solar energy refrigerator car of engine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160210 |