CN107816815A - Cold air circulating device - Google Patents
Cold air circulating device Download PDFInfo
- Publication number
- CN107816815A CN107816815A CN201610819367.5A CN201610819367A CN107816815A CN 107816815 A CN107816815 A CN 107816815A CN 201610819367 A CN201610819367 A CN 201610819367A CN 107816815 A CN107816815 A CN 107816815A
- Authority
- CN
- China
- Prior art keywords
- pipeline
- cold air
- air circulation
- condenser
- degree
- 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.)
- Pending
Links
- 239000003507 refrigerant Substances 0.000 claims abstract description 43
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 239000002826 coolant Substances 0.000 claims 3
- 238000010025 steaming Methods 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 abstract description 6
- 239000006260 foam Substances 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
Description
技术领域technical field
本发明是有关于一种冷气循环装置,特别是有关于一种利用液态及气态的分子撞击来产生低压的气态冷媒,进而可降低压缩机负载以达到节能省电功效的冷气循环装置。The present invention relates to a cold air circulation device, in particular to a cold air circulation device which utilizes liquid and gaseous molecules to collide to generate low-pressure gaseous refrigerant, thereby reducing the load of a compressor to achieve energy-saving and power-saving effects.
背景技术Background technique
由于现代人非常重视环境的舒适性,因此目前冷气循环装置为常见的电子设备,其可提供冷暖气至一空间中,使该空间中的温度能维持于使用者感觉舒适的温度。Because modern people attach great importance to the comfort of the environment, the current cooling air circulation device is a common electronic device, which can provide cooling and heating to a space, so that the temperature in the space can be maintained at a comfortable temperature for users.
如图1所示,其为其中一种习知技术的冷气循环装置的示意图。该习知的冷气循环装置包含有压缩机1、冷凝器2、蒸发器3、复数个过滤器4及电子膨胀阀5,且冷凝器2与蒸发器3分别接设一风扇马达6。其中,电子膨胀阀5装设在蒸发器3的入口端,其可用以将液态冷媒转换成气态样,并可减低冷媒的压力,以使进入蒸发器3的冷媒可在低压状况下易于蒸发。然而,虽然电子膨胀阀5可达到冷媒转换及降压的功用,但其仅可用以将纯液态的冷媒转换成气态,使得压缩机1仍需提供大量的压缩气体予冷凝器2,再由冷凝器2将压缩气体形成高压的液态冷媒,如此一来,压缩机1不但无法减轻其负载,亦将使得该冷气循环装置较为耗能耗电。As shown in FIG. 1 , it is a schematic diagram of a cold air circulation device in the prior art. The conventional cold air cycle device includes a compressor 1, a condenser 2, an evaporator 3, a plurality of filters 4 and an electronic expansion valve 5, and the condenser 2 and the evaporator 3 are respectively connected with a fan motor 6. Wherein, the electronic expansion valve 5 is installed at the inlet end of the evaporator 3, which can be used to convert the liquid refrigerant into a gaseous state, and can reduce the pressure of the refrigerant so that the refrigerant entering the evaporator 3 can be easily evaporated under low pressure. However, although the electronic expansion valve 5 can achieve the function of refrigerant conversion and pressure reduction, it can only be used to convert the pure liquid refrigerant into a gaseous state, so that the compressor 1 still needs to provide a large amount of compressed gas to the condenser 2, and then condensed The compressor 2 turns the compressed gas into a high-pressure liquid refrigerant. In this way, the compressor 1 not only cannot reduce its load, but also makes the cold air cycle device consume more energy and electricity.
此外,另有一种习知的冷气循环装置采用毛细管来进行冷媒转换及降压,然而该毛细管同样具有仅可将液态的冷媒转换成气态的缺点,使得压缩机无法降低运作负载。In addition, another conventional cold air cycle device uses capillary tubes to convert and decompress refrigerants. However, the capillary tubes also have the disadvantage of only converting liquid refrigerants into gaseous states, so that the compressor cannot reduce the operating load.
发明内容Contents of the invention
有鉴于上述习知技艺的问题,本发明的目的就是在提供一种利用液态及气态的分子撞击来产生低压的气态冷媒,进而可降低压缩机负载以达到节能省电功效的冷气循环装置。In view of the above-mentioned problems in the prior art, the object of the present invention is to provide a cold air cycle device that utilizes molecular collisions of liquid and gas to generate low-pressure gaseous refrigerant, thereby reducing the load of the compressor to save energy and power.
根据本发明的目的,提出一种冷气循环装置,其包含一压缩机、一冷凝器、至少一蒸发器、一储液器、至少一撞击区、至少一第一管路及至少一第二管路。压缩机的入口端衔接蒸发器的出口端,压缩机的出口端衔接冷凝器的入口端,冷凝器的出口端衔接储液器,第一管路及第二管路的一端衔接储液器,第一管路及第二管路的另一端衔接撞击区,且撞击区衔接蒸发器的入口端。其中,第一管路与第二管路的一端分别插入至撞击区中并形成一特定夹角,当第一管路与第二管路分别将储液器中的气态冷媒与液态冷媒输送至撞击区时,撞击区中的气态冷媒与液态冷媒相互分子撞击以产生一泡沫状饱和气态冷媒并输出至蒸发器。According to the object of the present invention, a cold air circulation device is proposed, which includes a compressor, a condenser, at least one evaporator, a liquid reservoir, at least one impact zone, at least one first pipeline and at least one second pipe road. The inlet of the compressor is connected to the outlet of the evaporator, the outlet of the compressor is connected to the inlet of the condenser, the outlet of the condenser is connected to the liquid receiver, and one end of the first pipeline and the second pipeline are connected to the liquid receiver. The other ends of the first pipeline and the second pipeline are connected to the impingement area, and the impingement area is connected to the inlet end of the evaporator. Wherein, one end of the first pipeline and the second pipeline are respectively inserted into the impact zone and form a specific angle, when the first pipeline and the second pipeline transport the gaseous refrigerant and the liquid refrigerant in the accumulator to the During the collision zone, the gaseous refrigerant and the liquid refrigerant in the collision zone collide with each other to produce a foamy saturated gaseous refrigerant which is output to the evaporator.
较佳地,上述特定夹角可为45度至185度。Preferably, the above-mentioned specific included angle may be 45 degrees to 185 degrees.
较佳地,上述特定夹角可为85度至185度。Preferably, the above-mentioned specific included angle may be 85 degrees to 185 degrees.
较佳地,上述特定夹角可为90度至180度。Preferably, the above-mentioned specific included angle may be 90 degrees to 180 degrees.
较佳地,上述特定夹角可为45度。Preferably, the above-mentioned specific included angle may be 45 degrees.
较佳地,上述特定夹角可为90度。Preferably, the above-mentioned specific included angle may be 90 degrees.
较佳地,上述第一管路与第二管路于撞击区中的管口距离可为0至8mm。Preferably, the nozzle distance between the first pipeline and the second pipeline in the impact zone may be 0 to 8 mm.
较佳地,上述第一管路与第二管路于撞击区中的管口距离可为0至5mm。Preferably, the nozzle distance between the first pipeline and the second pipeline in the impact zone may be 0 to 5 mm.
较佳地,上述特定夹角可为180度。Preferably, the above-mentioned specific included angle may be 180 degrees.
较佳地,上述第一管路与第二管路于撞击区中的管口距离可为1至8mm。Preferably, the nozzle distance between the first pipeline and the second pipeline in the impact zone may be 1 to 8 mm.
较佳地,上述第一管路与第二管路于撞击区中的管口距离可为1至5mm。Preferably, the nozzle distance between the first pipeline and the second pipeline in the impact zone may be 1 to 5 mm.
较佳地,此冷气循环装置更包含至少一第三管路,且撞击区、第一管路及第二管路的数量可为复数个,其中,各撞击区分别配接一个第一管路及第二管路,且二个的撞击区之间衔接一个第三管路。Preferably, the cold air circulation device further includes at least one third pipeline, and the number of impact areas, first pipelines and second pipelines can be multiple, wherein each impact area is respectively connected with a first pipeline And the second pipeline, and a third pipeline is connected between the two impact areas.
较佳地,此冷气循环装置更包含一滤网,衔接设置于冷凝器与储液器之间。Preferably, the cold air circulation device further includes a filter screen connected between the condenser and the liquid receiver.
较佳地,此冷气循环装置更包含一液气分离器,衔接设置于压缩机与蒸发器之间。Preferably, the cold air circulation device further includes a liquid-gas separator connected between the compressor and the evaporator.
较佳地,冷凝器及蒸发器分别配接一风扇马达。Preferably, the condenser and the evaporator are respectively equipped with a fan motor.
附图说明Description of drawings
图1为习知技术的冷气循环装置的示意图。FIG. 1 is a schematic diagram of a cold air circulation device in the prior art.
图2为本发明的冷气循环装置的一实施例的示意图。FIG. 2 is a schematic diagram of an embodiment of the cold air circulation device of the present invention.
图3为本发明的冷气循环装置的另一实施例的示意图。FIG. 3 is a schematic diagram of another embodiment of the cold air circulation device of the present invention.
图4为本发明的冷气循环装置的第一管路及第二管路配接至撞击区的第一示意图。FIG. 4 is a first schematic view of the first pipeline and the second pipeline of the cold air circulation device connected to the impact area of the present invention.
图5为本发明的冷气循环装置的第一管路及第二管路配接至撞击区的第二示意图。5 is a second schematic view of the first pipeline and the second pipeline of the cold air circulation device of the present invention being connected to the impact area.
图6为本发明的冷气循环装置的第一管路及第二管路配接至撞击区的第三示意图。FIG. 6 is a third schematic view of the first pipeline and the second pipeline of the cold air circulation device connected to the impact zone of the present invention.
图7为本发明的冷气循环装置的第一管路、第二管路及第三管路配接至撞击区的示意图。7 is a schematic diagram of the first pipeline, the second pipeline and the third pipeline of the cold air circulation device of the present invention being connected to the impact area.
图号说明:Description of figure number:
1、10 压缩机1, 10 Compressor
2、20 冷凝器2, 20 condenser
3、30 蒸发器3.30 evaporator
4 过滤器4 filters
5 电子膨胀阀5 Electronic expansion valve
6、100 风扇马达6. 100 fan motor
40 储液器40 reservoir
50 撞击区50 impact zone
60 第一管路60 first line
70 第二管路70 Second Line
80 滤网80 filter
90 液气分离器90 liquid gas separator
200 第三管路200 third line
A、B 阀门A and B valves
C 管口距离。C Nozzle distance.
具体实施方式Detailed ways
本发明的冷气循环装置主要利用储液器来储存冷凝器产生输出的液态冷媒及气态冷媒,再由第一管路及第二管路分别将气态冷媒与液态冷媒导流至撞击区,使得气态冷媒与液态冷媒在撞击区中得以相互分子撞击以产生泡沫式饱和气态冷媒,进而提供蒸发器进行潜热变化的所需,其中,本发明透过储液器、第一管路、第二管路及撞击区的组成来取代习知常见使用的电子膨胀阀、毛细管等构件,除了可执行冷媒形态转换与降压的功能外,由于其可利用液态加上气态的高压冷媒来进行转换成低压泡沫气态冷媒,而非习知仅可将液态转换成气态冷媒,这不但可将压缩机的运作负载降低,还可同时减少冷凝器的热排放。The cold air circulation device of the present invention mainly uses the liquid receiver to store the liquid refrigerant and the gaseous refrigerant produced by the condenser, and then guides the gaseous refrigerant and the liquid refrigerant to the impact area through the first pipeline and the second pipeline, so that the gaseous refrigerant The refrigerant and the liquid refrigerant can collide with each other in the collision zone to produce foamy saturated gaseous refrigerant, and then provide the evaporator with the latent heat change. And the composition of the impact zone to replace the commonly used electronic expansion valves, capillary tubes and other components, in addition to performing the function of refrigerant form conversion and pressure reduction, because it can use liquid and gaseous high-pressure refrigerant to convert into low-pressure foam The gaseous refrigerant, instead of the conventional liquid can only be converted into a gaseous refrigerant, which not only reduces the operating load of the compressor, but also reduces the heat discharge of the condenser at the same time.
本发明详细的结构,请参阅图2,其为本发明的冷气循环装置的一实施例的示意图,并请同时参阅图4、图5及图6,其分别为本发明的冷气循环装置的第一管路及第二管路配接至撞击区的第一示意图、第二示意图及第三示意图。本发明的冷气循环装置主要包含有压缩机10、冷凝器20、蒸发器30、储液器40、撞击区50、第一管路60及第二管路70,压缩机10的入口端衔接蒸发器30的出口端,压缩机10的出口端衔接冷凝器20的入口端,冷凝器20的出口端衔接储液器40,第一管路60及第二管路70的一端衔接储液器40,第一管路60及第二管路70的另一端衔接撞击区50,且撞击区50衔接蒸发器30的入口端,进而形成一套冷气循环回路。进一步地,本发明还包含有滤网80、液气分离器90及风扇马达100,滤网80衔接设置于冷凝器20与储液器40之间,其可用以进行杂质过滤,而液气分离器90衔接设置于压缩机10与蒸发器30之间,二个风扇马达100则分别配接至冷凝器20及蒸发器30。本发明的主要技术特征在于,储液器40、撞击区50、第一管路60及第二管路70共构形成一冷媒转换及降压系统,藉以可取代电子膨胀阀或毛细管,其中,第一管路60与第二管路70的一端分别插入至撞击区50中并形成一特定夹角,当第一管路60与第二管路70分别将储液器40中高压的气态冷媒与液态冷媒输送导流至撞击区50时,撞击区50中的气态冷媒与液态冷媒将会相互分子撞击以产生一低压的泡沫状饱和气态冷媒,再由该撞击区50将该泡沫状饱和气态冷媒输出至蒸发器30,让蒸发器30可藉由该泡沫状饱和气态冷媒达到较佳的吸热效果。For the detailed structure of the present invention, please refer to Fig. 2, which is a schematic diagram of an embodiment of the cold air circulation device of the present invention, and please refer to Fig. 4, Fig. 5 and Fig. A pipeline and a second pipeline are connected to the first schematic diagram, the second schematic diagram and the third schematic diagram of the impact zone. The cold air circulation device of the present invention mainly includes a compressor 10, a condenser 20, an evaporator 30, a liquid accumulator 40, an impact zone 50, a first pipeline 60 and a second pipeline 70, and the inlet end of the compressor 10 is connected to the evaporator The outlet end of the compressor 30, the outlet end of the compressor 10 is connected to the inlet end of the condenser 20, the outlet end of the condenser 20 is connected to the accumulator 40, and one end of the first pipeline 60 and the second pipeline 70 is connected to the accumulator 40 The other ends of the first pipeline 60 and the second pipeline 70 are connected to the impingement zone 50, and the impingement zone 50 is connected to the inlet end of the evaporator 30, thereby forming a cold air circulation loop. Further, the present invention also includes a filter screen 80, a liquid-gas separator 90, and a fan motor 100. The filter screen 80 is connected between the condenser 20 and the liquid receiver 40, and it can be used to filter impurities and separate liquid and gas. The compressor 90 is connected between the compressor 10 and the evaporator 30, and the two fan motors 100 are respectively connected to the condenser 20 and the evaporator 30. The main technical feature of the present invention is that the liquid accumulator 40, the impact area 50, the first pipeline 60 and the second pipeline 70 are jointly configured to form a refrigerant conversion and decompression system, so as to replace the electronic expansion valve or capillary tube, wherein, One end of the first pipeline 60 and one end of the second pipeline 70 are respectively inserted into the impingement zone 50 and form a specific included angle. When the liquid refrigerant is transported and diverted to the impact area 50, the gas refrigerant and the liquid refrigerant in the impact area 50 will collide with each other to generate a low-pressure foam-like saturated gas refrigerant, and then the foam-like saturated gas state will be formed by the impact area 50. The refrigerant is output to the evaporator 30 so that the evaporator 30 can achieve a better heat absorption effect through the foamy saturated gaseous refrigerant.
上述中,第一管路60与第二管路70于撞击区50中所形成的特定夹角可为45度至185度,或可为85度至185度,亦或是较佳可为90度至180度;例如,在图4及图6中,第一管路60与第二管路70的夹角分别形成90度与45度,且其中,第一管路60与第二管路70于撞击区50中的管口距离C可为0至8mm,较佳可为0至5mm;在图中5,第一管路60与第二管路70的夹角则可形成180度,且其中,第一管路60与第二管路70于撞击区50中的管口距离C可为1至8mm,较佳可为1至5mm。Among the above, the specific included angle formed by the first pipeline 60 and the second pipeline 70 in the impact zone 50 may be 45° to 185°, or 85° to 185°, or preferably 90° degrees to 180 degrees; for example, in Fig. 4 and Fig. 6, the included angles of the first pipeline 60 and the second pipeline 70 form 90 degrees and 45 degrees respectively, and wherein, the first pipeline 60 and the second pipeline The nozzle distance C of 70 in the impact zone 50 can be 0 to 8 mm, preferably 0 to 5 mm; in Figure 5, the angle between the first pipeline 60 and the second pipeline 70 can form 180 degrees, And wherein, the nozzle distance C between the first pipeline 60 and the second pipeline 70 in the impact area 50 may be 1 to 8 mm, preferably 1 to 5 mm.
接续,请参阅图3,其为本发明的冷气循环装置的另一实施例的示意图,并请同时参阅图7,其为本发明的冷气循环装置的第一管路、第二管路及第三管路配接至撞击区的示意图。本发明的冷气循环装置的撞击区50、第一管路60及第二管路70的数量可为复数个,各撞击区50分别配接一个第一管路60及第二管路70,而各撞击区50则可分别进一步配接一个蒸发器,如此一来,即可形成一对多的冷气系统。更进一步地,本发明的冷气循环装置还可包含至少一第三管路200,藉由控制阀门A或阀门B使其任一关闭时,该第三管路200可衔接在二个撞击区50之间,如此一来,透过该第三管路200可增加各撞击区50的分子撞击磨擦,进而提升冷媒形态转换的效果。在此实施例中,第一管路60与第二管路70、第三管路200的夹角分别可为90度,而第二管路70与第三管路200的夹角可为180度,如第7图所示,且第一管路60与第二管路70的管口之间所形成的分子撞击区与第三管路200的管口的距离可为0至8mm,较佳可为0至5mm。Continue, please refer to Fig. 3, which is a schematic diagram of another embodiment of the cold air circulation device of the present invention, and please refer to Fig. 7 at the same time, which is the first pipeline, the second pipeline and the first pipeline of the cold air circulation device of the present invention Schematic diagram of three tubing mated to the impact zone. The number of the impact zone 50, the first pipeline 60 and the second pipeline 70 of the cold air circulation device of the present invention can be multiple, and each impact zone 50 is respectively matched with a first pipeline 60 and a second pipeline 70, and Each impact area 50 can be further equipped with an evaporator, so that a one-to-many air-conditioning system can be formed. Furthermore, the cold air circulation device of the present invention may also include at least one third pipeline 200, and when either valve A or valve B is closed by controlling the valve A or valve B, the third pipeline 200 may be connected to the two impact areas 50 In this way, through the third pipeline 200 , the collision friction of molecules in each collision zone 50 can be increased, thereby improving the effect of refrigerant form conversion. In this embodiment, the angles between the first pipeline 60 and the second pipeline 70 and the third pipeline 200 can be 90 degrees respectively, and the angle between the second pipeline 70 and the third pipeline 200 can be 180 degrees. degree, as shown in Fig. 7, and the distance between the molecular collision zone formed between the nozzle of the first pipeline 60 and the nozzle of the second pipeline 70 and the nozzle of the third pipeline 200 can be 0 to 8mm, compared Preferably it can be 0 to 5mm.
综上所述,本发明的冷气循环装置透过储液器、第一管路、第二管路及撞击区的组成来取代习知所使用的电子膨胀阀与毛细管具有下列多数个优点。To sum up, the cold air circulation device of the present invention replaces the conventional electronic expansion valve and capillary tube through the composition of the liquid reservoir, the first pipeline, the second pipeline and the impact zone, and has the following advantages.
1、可降低压缩机负载,以达到节能省电的功效。1. It can reduce the load of the compressor to achieve the effect of saving energy and electricity.
2、冷凝器可减少热排放,进而可降低排碳量。2. The condenser can reduce heat emission, which in turn can reduce carbon emission.
3、提升潜热交换,使蒸发器吸热效果更佳。3. Improve the latent heat exchange, so that the evaporator has a better heat absorption effect.
4、可提升冷气循环装置整体设备的使用寿命,特别是压缩机及冷凝器。4. It can improve the service life of the overall equipment of the cold air circulation device, especially the compressor and condenser.
5. 冷气循环装置系统压力较低时,减少安装施工泄漏冷媒问题。5. When the system pressure of the cold air circulation device is low, the problem of refrigerant leakage during installation and construction can be reduced.
Claims (15)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610819367.5A CN107816815A (en) | 2016-09-13 | 2016-09-13 | Cold air circulating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610819367.5A CN107816815A (en) | 2016-09-13 | 2016-09-13 | Cold air circulating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107816815A true CN107816815A (en) | 2018-03-20 |
Family
ID=61601129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610819367.5A Pending CN107816815A (en) | 2016-09-13 | 2016-09-13 | Cold air circulating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107816815A (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2397951Y (en) * | 1999-10-10 | 2000-09-27 | 大连保税区荣昌消防设备工程有限公司 | Foam generator |
| JP2002181434A (en) * | 2001-12-03 | 2002-06-26 | Sharp Corp | Freezer refrigerator |
| US20050166621A1 (en) * | 1999-10-22 | 2005-08-04 | David Smolinsky | Heating and refrigeration systems and methods using refrigerant mass flow |
| CN1849487A (en) * | 2003-09-22 | 2006-10-18 | 拉斯·克里斯汀·伍尔夫·齐默曼 | Loop with Two-Step Capillary Restriction and Reservoir |
| JP2012093054A (en) * | 2010-10-28 | 2012-05-17 | Mitsubishi Electric Corp | Refrigerating apparatus |
| CN103211543A (en) * | 2013-04-10 | 2013-07-24 | 苏欢 | Integrated shower room with hot water supply system |
| WO2015050514A1 (en) * | 2013-10-03 | 2015-04-09 | Arcelik Anonim Sirketi | A cooling device comprising a flow regulator |
| KR20160005155A (en) * | 2014-07-03 | 2016-01-14 | 한온시스템 주식회사 | Cooling system of air conditioner for vehicle |
| CN105723164A (en) * | 2013-10-29 | 2016-06-29 | 大金工业株式会社 | Air conditioning device |
| CN206055990U (en) * | 2016-09-13 | 2017-03-29 | 饶秋金 | cold air circulating device |
-
2016
- 2016-09-13 CN CN201610819367.5A patent/CN107816815A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2397951Y (en) * | 1999-10-10 | 2000-09-27 | 大连保税区荣昌消防设备工程有限公司 | Foam generator |
| US20050166621A1 (en) * | 1999-10-22 | 2005-08-04 | David Smolinsky | Heating and refrigeration systems and methods using refrigerant mass flow |
| JP2002181434A (en) * | 2001-12-03 | 2002-06-26 | Sharp Corp | Freezer refrigerator |
| CN1849487A (en) * | 2003-09-22 | 2006-10-18 | 拉斯·克里斯汀·伍尔夫·齐默曼 | Loop with Two-Step Capillary Restriction and Reservoir |
| JP2012093054A (en) * | 2010-10-28 | 2012-05-17 | Mitsubishi Electric Corp | Refrigerating apparatus |
| CN103211543A (en) * | 2013-04-10 | 2013-07-24 | 苏欢 | Integrated shower room with hot water supply system |
| WO2015050514A1 (en) * | 2013-10-03 | 2015-04-09 | Arcelik Anonim Sirketi | A cooling device comprising a flow regulator |
| CN105723164A (en) * | 2013-10-29 | 2016-06-29 | 大金工业株式会社 | Air conditioning device |
| KR20160005155A (en) * | 2014-07-03 | 2016-01-14 | 한온시스템 주식회사 | Cooling system of air conditioner for vehicle |
| CN206055990U (en) * | 2016-09-13 | 2017-03-29 | 饶秋金 | cold air circulating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102954631A (en) | Refrigerating system | |
| CN108679868B (en) | A self-operated multifunctional heat pump system and its control method | |
| CN201697394U (en) | A heat recovery type multi-connected heat pump air conditioner with a hot water machine | |
| CN109269136B (en) | Air Conditioning System | |
| CN102032726A (en) | Air conditioner capable of improving low-temperature heating capacity | |
| CN205351844U (en) | Changes in temperature type air conditioning system and single cold mould air conditioning system | |
| CN203605512U (en) | Air-cooling type compression condensing unit with supercooled gas-liquid separator | |
| CN202304061U (en) | Air-source heat pump air conditioner with enhanced vapour injection (EVI) | |
| CN202382470U (en) | R32 air-cooled water chiller heat pump unit with EVI (enhanced vapor injection) compressor | |
| CN202581553U (en) | Air conditioner system | |
| CN205102289U (en) | Enhanced vapor injection air conditioning system | |
| CN101737998B (en) | Absorption type refrigerating unit for fully recovering waste heat | |
| CN101576328B (en) | An Air Conditioner with Large Subcooling Degree | |
| CN202382469U (en) | R32 air-cooling cold-water heat pump unit with liquid-spraying compressor | |
| CN204665732U (en) | A kind of refrigeration system | |
| CN107990581A (en) | A kind of electric automobile carbon dioxide heat-pump air-conditioning system | |
| CN107816815A (en) | Cold air circulating device | |
| CN102778081A (en) | Multilevel heat pump system | |
| CN207635639U (en) | A kind of electric vehicle carbon dioxide heat-pump air-conditioning system | |
| CN105972852A (en) | Air conditioning system | |
| CN201246918Y (en) | Novel ultra-low temperature air conditioner heat pump system | |
| CN103277930B (en) | Double-compressor energy-saving air conditioner | |
| CN203053083U (en) | Heat recovery type module type air-cooled water chilling unit | |
| CN206055990U (en) | cold air circulating device | |
| CN208254007U (en) | A kind of self-balance type cold and heat combined supply heat pump unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180320 |
|
| WD01 | Invention patent application deemed withdrawn after publication |