JPH09273876A - Cooler with natural circulation loop - Google Patents
Cooler with natural circulation loopInfo
- Publication number
- JPH09273876A JPH09273876A JP8084889A JP8488996A JPH09273876A JP H09273876 A JPH09273876 A JP H09273876A JP 8084889 A JP8084889 A JP 8084889A JP 8488996 A JP8488996 A JP 8488996A JP H09273876 A JPH09273876 A JP H09273876A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- refrigerant liquid
- liquid
- condenser
- gas
- 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 177
- 239000007788 liquid Substances 0.000 claims abstract description 152
- 238000001816 cooling Methods 0.000 claims abstract description 35
- 230000014759 maintenance of location Effects 0.000 claims abstract description 6
- 238000005057 refrigeration Methods 0.000 claims description 21
- 230000006835 compression Effects 0.000 claims description 13
- 238000007906 compression Methods 0.000 claims description 13
- 230000005484 gravity Effects 0.000 claims description 9
- 230000008016 vaporization Effects 0.000 claims description 3
- 238000009834 vaporization Methods 0.000 claims description 3
- 239000007791 liquid phase Substances 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 8
- 230000003247 decreasing effect Effects 0.000 description 5
- 239000002826 coolant Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 238000004781 supercooling Methods 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 2
- 230000001052 transient effect Effects 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000010295 mobile communication 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
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
-
- 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
- F25B23/00—Machines, plants or systems, with a single mode of operation not covered by groups F25B1/00 - F25B21/00, e.g. using selective radiation effect
- F25B23/006—Machines, plants or systems, with a single mode of operation not covered by groups F25B1/00 - F25B21/00, e.g. using selective radiation effect boiling cooling systems
-
- 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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/04—Refrigeration circuit bypassing means
- F25B2400/0401—Refrigeration circuit bypassing means for the compressor
-
- 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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/04—Refrigeration circuit bypassing means
- F25B2400/0411—Refrigeration circuit bypassing means for the expansion valve or capillary tube
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は自然循環ループを
備えた冷房装置に関し、特に熱交換効率を確保し冷房能
力を向上する凝縮器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling device having a natural circulation loop, and more particularly to a condenser for ensuring heat exchange efficiency and improving cooling capacity.
【0002】[0002]
【従来の技術】近年、冷房装置の用途は、人間を対象と
する対人空調だけでなく、電算機室や移動体通信の中継
電子機器を納めたカプセルなどに代表されるような電子
機器の発生した熱を除去する用途分野が急速に拡がりつ
つある。2. Description of the Related Art In recent years, air conditioners have been used not only for interpersonal air conditioning for humans, but also for electronic devices such as computer rooms and capsules containing relay electronic devices for mobile communication. The field of application for removing the generated heat is rapidly expanding.
【0003】これらの用途では室内で発生する熱負荷に
加えて、夏期等では外界から伝導する熱負荷(スキン・
ロード)がある。そこでこの室内に対する冷房能力は夏
期等を基準として設計され、冷房される空間を断熱壁で
囲いスキン・ロードを低減するとともに、その内部を冷
房能力の高い蒸気圧縮冷凍サイクルで冷房することが行
われる。一方、室内を断熱壁で囲ったため、冬期、夜間
のように外界が寒冷であっても室内機器から発生した熱
は外部へ散逸しにくく、室内温度が上昇する。このた
め、この室内に対しては寒冷な時期においても冷房が必
要となる。In these applications, in addition to the heat load generated indoors, the heat load (skin,
There is a road). Therefore, the cooling capacity for this room is designed based on summer, etc., and the space to be cooled is surrounded by a heat insulating wall to reduce the skin load and the inside is cooled by a vapor compression refrigeration cycle with high cooling capacity. . On the other hand, since the room is surrounded by a heat insulating wall, the heat generated from the indoor equipment is unlikely to be dissipated to the outside even if the outside environment is cold, such as in winter and at night, and the room temperature rises. For this reason, it is necessary to cool the room even in cold weather.
【0004】しかし、本来、自然放熱が可能な時期にお
いても、圧縮機運転動力の経費が高い蒸気圧縮冷凍サイ
クルをわざわざ使用するのは不経済であるし、圧縮機の
耐用年数、すなわち寿命が短くなるという問題とがあっ
た。このような場合には、内外の気温差を利用し、内部
から外部へ冷媒により伝熱するヒートパイプを用いるの
がよい。自然循環ループを用いた冷房サイクルは、この
ヒートパイプの原理を応用したものであり、冷媒ガスと
冷媒液とを別々の配管に通すことにより冷媒ループを形
成し、より高い伝熱効率を達成するものである。However, it is uneconomical to purposely use a vapor compression refrigeration cycle in which the operating cost of the compressor is high even when natural heat dissipation is possible, and the useful life of the compressor, that is, its life is short. There was a problem of becoming. In such a case, it is preferable to use a heat pipe that uses the temperature difference between the inside and the outside to transfer heat from the inside to the outside with a refrigerant. A cooling cycle using a natural circulation loop is an application of the principle of this heat pipe, and a refrigerant loop is formed by passing a refrigerant gas and a refrigerant liquid through separate pipes to achieve higher heat transfer efficiency. Is.
【0005】図5は、自然循環ループを用いた冷房装置
の原理を説明する模式的な構成図である。自然循環ルー
プでは、凝縮器2は蒸発器4より所定の高位置に配置さ
れる。凝縮器2は寒冷な室外に置かれ、ガス配管6から
送り込まれた冷媒ガスから外気への放熱を行い、冷媒ガ
スを冷媒液に相変化させる。この冷媒液は重力により液
配管8を下降し、これに蓄積される。この液配管8に蓄
積された冷媒液に対し作用する重力が冷媒循環の駆動力
となる。冷媒液は熱負荷を有した室内の蒸発器4に重力
によって供給され、ここで冷媒ガスとなる。この冷媒ガ
スは、圧力の低いガス配管6側に導かれる。ガス配管6
の蒸発器4側は、冷媒ガスの発生源であり、一方、凝縮
器2側は冷媒ガスの吸収源であるので、ガス配管6には
圧力勾配が生じる。つまり、凝縮器2側のガス圧は蒸発
器4側より低いので、冷媒液に比べて比重の小さい冷媒
ガスはガス配管6を上昇し、凝縮器2に到達する。FIG. 5 is a schematic configuration diagram for explaining the principle of a cooling device using a natural circulation loop. In the natural circulation loop, the condenser 2 is arranged at a predetermined higher position than the evaporator 4. The condenser 2 is placed outside in a cold room, radiates heat from the refrigerant gas sent from the gas pipe 6 to the outside air, and changes the phase of the refrigerant gas into a refrigerant liquid. This refrigerant liquid descends in the liquid pipe 8 due to gravity and is accumulated therein. The gravity acting on the refrigerant liquid accumulated in the liquid pipe 8 serves as the driving force for circulating the refrigerant. The refrigerant liquid is gravity-supplied to the indoor evaporator 4 having a heat load, and becomes the refrigerant gas there. This refrigerant gas is guided to the gas pipe 6 side having a low pressure. Gas pipe 6
Since the evaporator 4 side is a refrigerant gas generation source and the condenser 2 side is a refrigerant gas absorption source, a pressure gradient is generated in the gas pipe 6. That is, since the gas pressure on the condenser 2 side is lower than that on the evaporator 4 side, the refrigerant gas having a smaller specific gravity than the refrigerant liquid rises in the gas pipe 6 and reaches the condenser 2.
【0006】このように、自然循環ループの冷媒循環駆
動力は、凝縮器2と蒸発器4との高低差により生じ、よ
り正確には、液配管8中に蓄積される冷媒液柱の高さに
比例する。ループ中に存在する冷媒液の量(又は冷媒液
と冷媒ガスの比)は、室内と室外との温度差及び室外の
温度によって変化する。蒸気圧縮冷凍サイクルの場合に
は、圧縮機や膨張弁の動作を調節することにより、この
変化を抑制することもできる。しかし、自然循環ループ
においてはそのような調節機構がないので、冷媒液の量
は大きく変化する。As described above, the refrigerant circulation driving force of the natural circulation loop is generated by the height difference between the condenser 2 and the evaporator 4, and more accurately, the height of the refrigerant liquid column accumulated in the liquid pipe 8. Proportional to. The amount of the refrigerant liquid existing in the loop (or the ratio of the refrigerant liquid and the refrigerant gas) changes depending on the temperature difference between the room and the room and the temperature outside the room. In the case of the vapor compression refrigeration cycle, this change can be suppressed by adjusting the operations of the compressor and the expansion valve. However, in the natural circulation loop, since there is no such adjusting mechanism, the amount of the refrigerant liquid changes greatly.
【0007】なお、この自然循環ループは冷媒循環に圧
縮機を必要とせず上述した経済性等の利点を有するた
め、上記のように四季を通じて室内の冷房が必要とされ
る用途には、蒸気圧縮冷凍サイクルに自然循環ループを
併用した冷房装置が提案されている(特願平7−222
920)。この装置は、冷媒循環系を構成する流路の一
部を切り換えることにより、夏期等の熱負荷が高い場合
には蒸気圧縮冷凍サイクルを構成し、冬期等の熱負荷が
低い場合には自然循環ループを構成して冷房を行う。Since the natural circulation loop does not require a compressor for circulating the refrigerant and has the advantages of the above-described economy, the vapor compression is used for the applications requiring indoor cooling throughout the four seasons as described above. A cooling device using a natural circulation loop in a refrigeration cycle has been proposed (Japanese Patent Application No. 7-222).
920). This device forms a vapor compression refrigeration cycle when the heat load is high in summer, etc. by switching some of the flow paths that make up the refrigerant circulation system, and natural circulation when the heat load is low in winter etc. A loop is constructed to perform cooling.
【0008】[0008]
【発明が解決しようとする課題】上述したように自然循
環ループ内の冷媒液の量は、外気温の影響を受けて大き
く変動する。そのため、外気温が低いと冷媒液の量が増
加し、液配管に収容しきれない冷媒液が凝縮器に滞留す
ることが起こる。すると、凝縮器における冷媒ガスと外
気とが行われる有効な伝熱面積が減少して冷媒液の過冷
却量が減少し、この自然循環ループを用いた冷房装置の
冷房能力が低下するという問題点があった。As described above, the amount of the refrigerant liquid in the natural circulation loop fluctuates greatly under the influence of the outside temperature. Therefore, when the outside air temperature is low, the amount of the refrigerant liquid increases, and the refrigerant liquid that cannot be accommodated in the liquid pipe may stay in the condenser. Then, the effective heat transfer area where the refrigerant gas and the outside air are performed in the condenser is decreased, the amount of supercooling of the refrigerant liquid is decreased, and the cooling capacity of the cooling device using this natural circulation loop is reduced. was there.
【0009】また、蒸気圧縮冷凍サイクルと自然循環ル
ープを併用した上記のような冷房装置では、それら冷媒
循環系を切り換えることによっても冷媒液の量、又はそ
の分布が変化し、上記同様の冷房能力低下の問題が生じ
る場合がある。Further, in the above cooling apparatus using both the vapor compression refrigeration cycle and the natural circulation loop, the amount or distribution of the refrigerant liquid is changed by switching the refrigerant circulation systems, and the cooling capacity is the same as the above. Degradation problems may occur.
【0010】本発明は、冬期のように低外気温の場合や
冷媒循環系を自然循環ループに切り換えた場合に、凝縮
器に冷媒液が滞留することを抑制し、冷房能力の低下が
防止される自然循環ループを備えた冷房装置を提供する
ことを目的とする。The present invention suppresses the retention of the refrigerant liquid in the condenser when the outside temperature is low such as in winter or when the refrigerant circulation system is switched to the natural circulation loop, thereby preventing the cooling capacity from decreasing. An object of the present invention is to provide a cooling device having a natural circulation loop.
【0011】[0011]
【課題を解決するための手段】本発明の自然循環ループ
を備えた冷房装置は、冷媒液の流路に接続され、冷媒液
を溜めて前記凝縮器内部の冷媒液の滞留を除去する冷媒
液溜めを有することを特徴とする。本発明によれば冷媒
液溜めは、例えば、液配管途中における凝縮器と蒸発器
との間の高さ位置に配置されたり、別途設けられる管に
よってかかる液配管途中の位置に接続されたり、凝縮器
の下部に接続又は併設され、この冷媒液溜めが、凝縮器
で液化され液配管に蓄積される冷媒液量が液配管の容量
を超える場合でも、その過剰な冷媒液を溜めるので、冷
媒液は凝縮器から除去される。このため凝縮器に冷媒液
が滞留することが抑制され、よって凝縮器における冷媒
ガスと外気との伝熱面積が確保されて冷房能力の低下が
防止される。冷媒液溜めは、冷媒液量が多いときのみ冷
媒液を溜め、その溜められた冷媒液は、冷媒液の過剰が
解消される場合には、液配管中の冷媒液の量よりも先に
減少する。A cooling device provided with a natural circulation loop of the present invention is a refrigerant liquid which is connected to a flow path of a refrigerant liquid and accumulates the refrigerant liquid to remove retention of the refrigerant liquid inside the condenser. It is characterized by having a reservoir. According to the present invention, the refrigerant liquid reservoir is arranged, for example, at a height position between the condenser and the evaporator in the middle of the liquid pipe, or is connected to a position in the middle of the liquid pipe by a separately provided pipe, This refrigerant liquid reservoir, which is connected to or attached to the lower part of the condenser, collects excess refrigerant liquid even if the amount of refrigerant liquid liquefied in the condenser and accumulated in the liquid pipe exceeds the capacity of the liquid pipe. Is removed from the condenser. For this reason, the refrigerant liquid is suppressed from accumulating in the condenser, so that the heat transfer area between the refrigerant gas and the outside air in the condenser is ensured and the cooling capacity is prevented from being lowered. The refrigerant liquid reservoir collects the refrigerant liquid only when the amount of the refrigerant liquid is large, and the accumulated refrigerant liquid is reduced before the amount of the refrigerant liquid in the liquid pipe when the excess of the refrigerant liquid is eliminated. To do.
【0012】本発明の自然循環ループを備えた冷房装置
においては、前記冷媒液溜めは、前記凝縮器への液配管
の接続位置の高さに設けられることを特徴とする。本発
明によれば、凝縮器での冷媒液の滞留が抑制されながら
も液配管に蓄積される冷媒液柱の高さが高くなり、自然
循環ループにおける冷媒循環の駆動力が確保される。よ
って、凝縮器における伝熱面積の確保と駆動力の確保と
によって、一層高い冷房能力が実現される。In the cooling apparatus having the natural circulation loop of the present invention, the refrigerant liquid reservoir is provided at the height of the connection position of the liquid pipe to the condenser. According to the present invention, the height of the refrigerant liquid column accumulated in the liquid pipe is increased while the retention of the refrigerant liquid in the condenser is suppressed, and the driving force for refrigerant circulation in the natural circulation loop is secured. Therefore, by ensuring the heat transfer area and the driving force in the condenser, a higher cooling capacity is realized.
【0013】[0013]
【発明の実施の形態】次に、本発明の実施形態について
図面を参照して説明する。Next, embodiments of the present invention will be described with reference to the drawings.
【0014】[実施形態1]図1は、自然循環ループを
用いた本発明の冷房装置における冷凍サイクルの模式的
な構成図である。本装置は圧縮機を有しておらず自然循
環ループのみを用いている。[Embodiment 1] FIG. 1 is a schematic configuration diagram of a refrigeration cycle in a cooling device of the present invention using a natural circulation loop. This device does not have a compressor and uses only a natural circulation loop.
【0015】本装置における自然循環ループの原理は従
来技術の図5に示したものと同様であるので、同一の機
能を有する構成要素には、図5の符号に20を加えた符
号を付し説明を省略することがある。必要な冷媒循環駆
動力を得るため、凝縮器22は例えば約2mの高低差を
有した液配管28によって蒸発器24より高い位置に配
置される。本装置では、冷媒液溜め30が水平な支管3
2によって液配管28に接続されている。その接続位置
の高さは、液配管28の凝縮器22への接続位置であ
る。Since the principle of the natural circulation loop in this device is the same as that shown in FIG. 5 of the prior art, the components having the same functions are designated by the symbols of FIG. 5 plus 20. Description may be omitted. In order to obtain the necessary driving force for circulating the refrigerant, the condenser 22 is arranged at a higher position than the evaporator 24 by a liquid pipe 28 having a height difference of, for example, about 2 m. In this device, the refrigerant liquid reservoir 30 has a horizontal branch pipe 3
2 is connected to the liquid pipe 28. The height of the connecting position is the connecting position of the liquid pipe 28 to the condenser 22.
【0016】凝縮器22で生じた冷媒液は、重力により
液配管28を下降し、まずこれに蓄積される。しかし、
外気温が特に低い場合には、ループ中の冷媒液(つまり
気相状態ではなく液相状態の冷媒)の量が多くなり、液
配管28の上部まで冷媒液が充満し、さらに過剰な冷媒
液が発生することがある。The refrigerant liquid generated in the condenser 22 descends in the liquid pipe 28 due to gravity and is first accumulated therein. But,
When the outside air temperature is particularly low, the amount of the refrigerant liquid in the loop (that is, the refrigerant in the liquid phase state instead of the gas phase state) increases, and the upper portion of the liquid pipe 28 is filled with the refrigerant liquid. May occur.
【0017】従来はこの過剰な冷媒液は、凝縮器22内
の伝熱チューブの下部に滞留していた。これに対し本装
置では、過剰な冷媒液は凝縮器22と冷媒液溜め30と
で分配される。このとき、凝縮器22内と冷媒液溜め3
0内とにおける冷媒液面の高さは基本的には同一とな
る。ここで冷媒液溜め30は大きな底面積を有した容器
で構成されるのに対し、凝縮器22はその内部に伝熱チ
ューブが幾重にも折り曲がりながら冷媒ガスを上から下
へ導くように配管されている。このように細長い管の中
を冷媒を通すことにより外気との伝熱面積を大きくとる
ことができ、十分に冷却された冷媒液が得られる。すな
わち冷媒液の過冷却量を稼ぐことができる。この構造の
違いにより、凝縮器22と冷媒液溜め30との同一高さ
に蓄積できる液量については、冷媒液溜め30の方が十
分大きい。そのため、過剰な冷媒液の大半が冷媒液溜め
30に蓄積され、本装置における凝縮器22内の冷媒液
面の高さは冷媒液溜め30を用いない場合に比べて十分
に抑制される。Conventionally, this excess refrigerant liquid has accumulated in the lower portion of the heat transfer tube in the condenser 22. On the other hand, in this device, excess refrigerant liquid is distributed between the condenser 22 and the refrigerant liquid reservoir 30. At this time, the inside of the condenser 22 and the refrigerant reservoir 3
The height of the liquid surface of the refrigerant in the inside of 0 is basically the same. Here, while the refrigerant liquid reservoir 30 is composed of a container having a large bottom area, the condenser 22 has pipes for guiding the refrigerant gas from top to bottom while the heat transfer tubes are bent in multiple layers therein. Has been done. By passing the refrigerant through the elongated tube in this way, a large heat transfer area with the outside air can be obtained, and a sufficiently cooled refrigerant liquid can be obtained. That is, the amount of supercooling of the refrigerant liquid can be earned. Due to this difference in structure, the refrigerant liquid reservoir 30 has a sufficiently large amount of liquid that can be accumulated at the same height as the condenser 22 and the refrigerant liquid reservoir 30. Therefore, most of the excess refrigerant liquid is accumulated in the refrigerant liquid reservoir 30, and the height of the refrigerant liquid surface in the condenser 22 in this device is sufficiently suppressed as compared with the case where the refrigerant liquid reservoir 30 is not used.
【0018】凝縮器22内の液面高さが抑制されること
により、冷媒ガスと外気との熱交換が行われる有効な伝
熱チューブの長さ、又は有効な伝熱面積が大きくなる。
すなわち、熱交換の効率が向上し冷媒液の過冷却量が増
大することにより、冷房能力が向上する。By suppressing the liquid level in the condenser 22, the length of the effective heat transfer tube or the effective heat transfer area for heat exchange between the refrigerant gas and the outside air is increased.
That is, the efficiency of heat exchange is improved and the supercooling amount of the refrigerant liquid is increased, so that the cooling capacity is improved.
【0019】冷媒液面が支管32より低下する際に、冷
媒液溜め30内部に蓄積された冷媒液が速やかに液配管
28に流出するように、容器の下部に支管32が接続さ
れている。本装置の冷媒液溜め30の容器は十分に大き
いので上部を密閉構造としても問題ないが、小さな容器
の場合には容器上部を密閉構造とすると、液面34が上
昇するにつれ容器上部に形成される気相部分36の圧力
が高くなり、冷媒液が容器に流入しにくくなる。そのた
め、小さな容器では、気相部分36の気圧調整用の細管
を容器上部から例えば凝縮器22における気相部分の伝
熱チューブに接続したり、容器上部を外気へさらして放
熱を容易とし冷却によって気相部分36の気圧を下げる
といった構造としてもよい。The branch pipe 32 is connected to the lower portion of the container so that the coolant liquid accumulated in the coolant liquid reservoir 30 quickly flows out to the liquid pipe 28 when the coolant liquid level drops below the branch pipe 32. The container of the refrigerant liquid reservoir 30 of the present device is sufficiently large so that the upper part may have a closed structure. However, in the case of a small container, if the upper part of the container has a closed structure, the liquid surface 34 is formed on the upper part of the container as it rises. As a result, the pressure of the vapor phase portion 36 becomes high, and it becomes difficult for the refrigerant liquid to flow into the container. Therefore, in a small container, a thin tube for adjusting the atmospheric pressure of the gas phase portion 36 is connected from the upper portion of the container to, for example, a heat transfer tube of the gas phase portion of the condenser 22, or the upper portion of the container is exposed to the outside air to facilitate heat dissipation, thereby cooling The structure may be such that the atmospheric pressure of the vapor phase portion 36 is lowered.
【0020】本装置の冷媒液溜め30は、最大冷媒循環
駆動力を得るために必要とされる冷媒液柱の高さ、例え
ば2mを確保するため、液配管28の最高点に接続され
ている。ちなみに、冷媒液溜めは別の位置に設けること
もできる。図2、図3は、冷媒液溜めの他の設置形態を
示す冷凍サイクルの模式的構成を示す図(図2は部分
図)である。図2(a)に示される形態においては、冷
媒液溜め40は液配管28の途中かつその最高点に設け
られている点で上記装置と同様である。上記装置との相
違点は冷媒液溜め40の容器上部に冷媒流入口42、容
器下部に冷媒流出口44を個別に有していることであ
る。これにより、冷媒液溜め40における冷媒の流入・
流出が円滑に行われる。The refrigerant sump 30 of the present apparatus is connected to the highest point of the liquid pipe 28 in order to secure the height of the refrigerant liquid column required to obtain the maximum refrigerant circulation driving force, for example, 2 m. . Incidentally, the coolant reservoir may be provided at another position. 2 and 3 are diagrams (FIG. 2 is a partial view) showing a schematic configuration of a refrigerating cycle showing another installation mode of a refrigerant liquid reservoir. In the form shown in FIG. 2A, the refrigerant liquid reservoir 40 is similar to the above device in that it is provided in the middle of the liquid pipe 28 and at the highest point thereof. The difference from the above apparatus is that the refrigerant reservoir 40 has a refrigerant inlet 42 in the upper portion of the container and a refrigerant outlet 44 in the lower portion of the container. As a result, the inflow of the refrigerant into the refrigerant liquid reservoir 40
The outflow will be smooth.
【0021】図2(b)に示される形態においては、冷
媒液溜め50が凝縮器22に併設、すなわち液配管を介
さず直に凝縮器22に接続されている。図2(c)に示
される形態においては、冷媒液溜め60が凝縮器22の
下部の伝熱チューブ62に接続されている。In the embodiment shown in FIG. 2 (b), the refrigerant liquid reservoir 50 is provided side by side with the condenser 22, that is, directly connected to the condenser 22 without a liquid pipe. In the configuration shown in FIG. 2C, the refrigerant liquid reservoir 60 is connected to the heat transfer tube 62 below the condenser 22.
【0022】以上の形態はいずれも、冷媒循環駆動力を
与える冷媒液柱の高さを損ねないように、冷媒液溜めを
できるだけ高い位置に設けた。このように配置すること
は高い冷房能力を得るためには望ましいことであるが、
逆に他の理由で冷媒液柱の高さを制限すべき場合もあ
る。例えば蒸発器24が配置される被冷却部が、外界か
ら離れていて、凝縮器22の高さが非常に高くなるよう
な場合、その高さの冷媒液柱の圧力に蒸発器24の構造
が耐えられないこともあり得る。このような場合には、
図3(a)、(b)に示されるように、冷媒液溜め7
0、80を凝縮器22と蒸発器24との間の、例えば冷
媒駆動力の上限により定まる高さに配置する。これによ
り、凝縮器22に冷媒液が滞留しなくなるとともに、冷
媒液柱の高さ上限を冷媒液溜めの高さに設定することが
できる。In all of the above-mentioned embodiments, the refrigerant liquid reservoir is provided at a position as high as possible so as not to impair the height of the refrigerant liquid column that gives the refrigerant circulation driving force. Although this arrangement is desirable for obtaining high cooling capacity,
On the contrary, there are cases where the height of the refrigerant liquid column should be limited for other reasons. For example, when the portion to be cooled in which the evaporator 24 is arranged is separated from the outside world and the height of the condenser 22 becomes very high, the structure of the evaporator 24 is affected by the pressure of the refrigerant liquid column at that height. It can be unbearable. In such a case,
As shown in FIGS. 3A and 3B, the refrigerant liquid reservoir 7
0 and 80 are arranged between the condenser 22 and the evaporator 24, for example, at a height determined by the upper limit of the refrigerant driving force. As a result, the refrigerant liquid does not stay in the condenser 22, and the upper limit of the height of the refrigerant liquid column can be set to the height of the refrigerant liquid reservoir.
【0023】[実施形態2]図4は、本発明の他の実施
形態であって、蒸気圧縮冷凍サイクルに自然循環ループ
を併用した冷房装置における冷凍サイクルの模式的な構
成図である。この冷房装置における蒸気圧縮冷凍サイク
ルは、大まかには圧縮機100、凝縮器102、蒸発器
104、膨張弁106からなる。圧縮機100は、蒸発
器104で発生した冷媒ガスを導くガス配管108の途
中に設けられ、冷媒ガスを吸い込み、これを断熱的に圧
縮して送出する。これにより、冷媒ガスは過熱状態にさ
れるとともに、冷媒サイクルには冷媒循環の駆動力が供
給される。凝縮器102は過熱冷媒ガスから放熱させ、
これを液化する。冷媒液は液配管110を経由して蒸発
器104側に送られる。蒸発器104の手前に設けられ
た膨張弁106は、高圧の冷媒液を減圧して低圧で気液
混合状態の湿り蒸気とする機能を有する。湿り蒸気は蒸
発器104において被冷却物から気化熱を吸収して冷媒
ガスとなり、再びガス配管108へ送出される。なお、
サクションアキュムレータ112は運転の過渡的現象や
冷媒封入量過多などの場合に、緩衝の役割を果たす器で
ある。[Embodiment 2] FIG. 4 is another embodiment of the present invention, and is a schematic configuration diagram of a refrigeration cycle in a cooling apparatus in which a natural circulation loop is used in combination with a vapor compression refrigeration cycle. The vapor compression refrigeration cycle in this cooling device roughly includes a compressor 100, a condenser 102, an evaporator 104, and an expansion valve 106. The compressor 100 is provided in the middle of a gas pipe 108 that guides the refrigerant gas generated in the evaporator 104, sucks the refrigerant gas, adiabatically compresses it, and sends it out. As a result, the refrigerant gas is brought into an overheated state, and the driving force for circulating the refrigerant is supplied to the refrigerant cycle. The condenser 102 radiates heat from the overheated refrigerant gas,
This is liquefied. The refrigerant liquid is sent to the evaporator 104 side via the liquid pipe 110. The expansion valve 106 provided in front of the evaporator 104 has a function of reducing the pressure of the high-pressure refrigerant liquid to low-pressure wet vapor in a gas-liquid mixed state. The wet steam absorbs the heat of vaporization from the object to be cooled in the evaporator 104, becomes a refrigerant gas, and is sent out to the gas pipe 108 again. In addition,
The suction accumulator 112 is a device that acts as a buffer in the case of a transient phenomenon of operation or an excessive amount of refrigerant filled.
【0024】次に、自然循環ループを説明する。その大
半は以上述べた蒸気圧縮冷凍サイクルと共通である。自
然循環ループは、1つにはサクションアキュムレータ1
12と圧縮機100とをバイパスする点、もう1つには
膨張弁106をバイパスする点が蒸気圧縮冷凍サイクル
と異なる。自然循環ループはこれらのバイパスのためそ
れぞれバイパス管120、122を有している。これら
流路の切り換えは、切換弁124、126、128、1
30により行われる。すなわち、この冷凍サイクルを蒸
気圧縮冷凍サイクルとして使用する場合(強制循環モー
ドと称する)には、切換弁124、128を開き、切換
弁126、130を閉じる。逆に、冷凍サイクルを自然
循環ループとして使用する場合(自然循環モードと称す
る)には、切換弁126、130を開き、切換弁12
4、128を閉じる。Next, the natural circulation loop will be described. Most of them are common with the vapor compression refrigeration cycle described above. The natural circulation loop includes a suction accumulator 1
12 is different from the vapor compression refrigeration cycle in that the compressor 12 and the compressor 100 are bypassed and the expansion valve 106 is bypassed. The natural circulation loop has bypass pipes 120 and 122 for these bypasses, respectively. Switching of these flow paths is performed by switching valves 124, 126, 128, 1
30. That is, when this refrigeration cycle is used as a vapor compression refrigeration cycle (referred to as a forced circulation mode), the switching valves 124 and 128 are opened and the switching valves 126 and 130 are closed. On the contrary, when the refrigeration cycle is used as a natural circulation loop (referred to as a natural circulation mode), the switching valves 126 and 130 are opened and the switching valve 12 is opened.
4, 128 is closed.
【0025】本装置の自然循環ループも、上記実施形態
と同様、液配管110に蓄積される冷媒液に作用する重
力を冷媒循環の駆動力とする。冷媒液は重力により蒸発
器104に供給され、ここで冷媒ガスとなる。自然循環
ループではバイパス管120が冷媒ガスの流路となり、
比重の軽い冷媒ガスは圧縮機100を停止した状態にお
いてもガス配管108を上昇し凝縮器102に達し、凝
縮器102で冷媒液となる。In the natural circulation loop of this apparatus, as in the above embodiment, the gravity acting on the refrigerant liquid accumulated in the liquid pipe 110 is used as the driving force for the refrigerant circulation. The refrigerant liquid is supplied to the evaporator 104 by gravity and becomes a refrigerant gas here. In the natural circulation loop, the bypass pipe 120 serves as a refrigerant gas flow path,
The refrigerant gas having a low specific gravity rises in the gas pipe 108 even when the compressor 100 is stopped, reaches the condenser 102, and becomes a refrigerant liquid in the condenser 102.
【0026】本装置では流出口と流入口とを有する冷媒
液溜め132が、液配管110の途中であって液配管1
10が凝縮器102に接続される高さに設けられてい
る。この冷媒液溜めは、まず実施形態1同様の自然循環
モードでの低外気温時の過剰な冷媒液が凝縮器102内
に滞留するという現象を回避する働きがある。また本装
置ではこの現象とともに、強制循環モードから自然循環
モードにを切り換えた場合の冷媒循環系内での冷媒液の
分布や量の変化による冷媒液柱高さの変化に起因して、
冷媒液が凝縮器102内に滞留するいう現象が起こる可
能性がある。この現象を回避するために、運転モードの
切り換え時に、冷媒を出し入れして装置内の冷媒量を調
整するといった方法は、煩雑であり現実的ではない。冷
媒液溜め132は、そのような煩雑な操作をすることな
く、この現象も回避する働きを有するものである。この
冷媒液溜め132によって、本装置は外気温に係わら
ず、また運転モードの切り換え時に特別な操作をするこ
となく、上記両現象による凝縮器102の有効伝熱面積
の減少を防止でき、常に凝縮器102の性能が十分に発
揮された冷房能力を提供することができる。In this apparatus, a refrigerant liquid reservoir 132 having an outflow port and an inflow port is located in the middle of the liquid pipe 110 and is located in the liquid pipe 1.
10 is provided at a height connected to the condenser 102. First, this refrigerant liquid reservoir has a function of avoiding a phenomenon in which excessive refrigerant liquid accumulates in the condenser 102 at the time of low ambient temperature in the natural circulation mode similar to the first embodiment. In addition to this phenomenon in the present device, due to a change in the refrigerant liquid column height due to a change in the distribution and amount of the refrigerant liquid in the refrigerant circulation system when the forced circulation mode is switched to the natural circulation mode,
The phenomenon that the refrigerant liquid stays in the condenser 102 may occur. In order to avoid this phenomenon, the method of adjusting the amount of refrigerant in the device by taking in and out the refrigerant at the time of switching the operation mode is complicated and not realistic. The refrigerant liquid reservoir 132 has a function of avoiding this phenomenon without performing such a complicated operation. With this refrigerant liquid reservoir 132, the present device can prevent the effective heat transfer area of the condenser 102 from decreasing due to both of the above phenomena, regardless of the outside air temperature, and without performing a special operation at the time of switching the operation mode, and always condense. It is possible to provide the cooling capacity with which the performance of the container 102 is fully exhibited.
【0027】なお、サクションアキュムレータ112
も、冷媒液を蓄積することができるが、設けられる位置
がガス配管108側であり、その目的は冷媒液の調整と
いうより、圧縮機100の保護である。すなわち、例え
ば、過渡的状態で気化していない液が大量にガス配管に
入るといったことにより、圧縮機100に冷媒液が流入
すると、圧縮機100が破損する恐れがあるが、サクシ
ョンアキュムレータ112はこれを防止するものであ
り、冷媒液溜め132の上述したような機能を有しな
い。Incidentally, the suction accumulator 112
Also, although the refrigerant liquid can be accumulated, the position where it is provided is the gas pipe 108 side, and the purpose thereof is not to adjust the refrigerant liquid but to protect the compressor 100. That is, when the refrigerant liquid flows into the compressor 100 by, for example, a large amount of liquid that has not been vaporized in a transient state enters the gas pipe, the compressor 100 may be damaged. The refrigerant reservoir 132 does not have the above-described function.
【0028】[0028]
【発明の効果】本発明によれば、冬期のように低外気温
の場合や冷媒循環系を自然循環ループに切り換えた場合
において生じうる過剰な冷媒液は冷媒液溜めに溜めら
れ、凝縮器への滞留が抑制されるので、凝縮器の熱交換
効率が常に良好な値に維持され冷房能力の低下が防止さ
れるという効果がある。According to the present invention, excess refrigerant liquid that may be generated when the ambient temperature is low, such as in winter, or when the refrigerant circulation system is switched to the natural circulation loop, is accumulated in the refrigerant reservoir and is supplied to the condenser. As a result, the heat exchange efficiency of the condenser is always maintained at a good value and the cooling capacity is prevented from decreasing.
【図面の簡単な説明】[Brief description of drawings]
【図1】 自然循環ループを用いた本発明に係る冷房装
置における冷凍サイクルの模式的な構成図。FIG. 1 is a schematic configuration diagram of a refrigeration cycle in a cooling device according to the present invention using a natural circulation loop.
【図2】 冷媒液溜めの設置形態を示す冷凍サイクルの
模式的構成の部分図。FIG. 2 is a partial view of a schematic configuration of a refrigeration cycle showing an installation form of a refrigerant liquid reservoir.
【図3】 冷媒液溜めの設置形態を示す冷凍サイクルの
模式的構成図。FIG. 3 is a schematic configuration diagram of a refrigeration cycle showing an installation form of a refrigerant liquid reservoir.
【図4】 蒸気圧縮冷凍サイクルに自然循環ループを併
用した本発明に係る冷房装置における冷凍サイクルの模
式的な構成図。FIG. 4 is a schematic configuration diagram of a refrigeration cycle in a cooling device according to the present invention in which a natural circulation loop is used in combination with a vapor compression refrigeration cycle.
【図5】 自然循環ループを用いた従来技術の冷房装置
の原理を説明する模式的な構成図。FIG. 5 is a schematic configuration diagram illustrating the principle of a conventional cooling device using a natural circulation loop.
22,102 凝縮器、24,104 蒸発器、26,
108 ガス配管、28,110 液配管、30,13
2 冷媒液溜め、100 圧縮機、106 膨張弁、1
20,122 バイパス管。22,102 condenser, 24,104 evaporator, 26,
108 gas piping, 28,110 liquid piping, 30,13
2 Refrigerant reservoir, 100 compressor, 106 expansion valve, 1
20,122 Bypass pipe.
Claims (3)
冷却部から吸収する蒸発器と、この蒸発器に接続され冷
媒ガスを上昇させるガス配管と、このガス配管に接続さ
れこれにより導かれた冷媒ガスを液化して冷媒液とする
凝縮器と、この凝縮器に接続されこれにより生成された
冷媒液を重力によって下降させて前記蒸発器へ導く液配
管とを含む自然循環ループを備える冷房装置において、 前記冷媒液の流路に接続され、前記冷媒液を溜めて前記
凝縮器内部の冷媒液の滞留を除去する冷媒液溜めを有す
ることを特徴とする冷房装置。1. An evaporator for absorbing heat of vaporization when a refrigerant liquid becomes a refrigerant gas from a cooled portion, a gas pipe connected to the evaporator for raising the refrigerant gas, and connected to the gas pipe, thereby A natural circulation loop including a condenser that liquefies the introduced refrigerant gas into a refrigerant liquid, and a liquid pipe that is connected to this condenser and causes the refrigerant liquid generated by this to descend by gravity and guide it to the evaporator. An air conditioner provided with a refrigerant liquid reservoir which is connected to the flow path of the refrigerant liquid and which collects the refrigerant liquid and removes the retention of the refrigerant liquid inside the condenser.
冷却部から吸収する蒸発器と、この蒸発器に接続され冷
媒ガスを上昇させるガス配管と、このガス配管に接続さ
れこれにより導かれた冷媒ガスを液化して冷媒液とする
凝縮器と、この凝縮器に接続されこれにより生成された
冷媒液を重力によって下降させて前記蒸発器へ導く液配
管と、前記ガス配管の途中に挿入され冷媒ガスを断熱的
に圧縮する圧縮機と、これをバイパスする圧縮機バイパ
ス手段と、圧縮機と圧縮機バイパス手段とを切り換える
手段と、前記液配管の途中に挿入され冷媒液を減圧する
膨張弁と、これをバイパスする膨張弁バイパス手段と、
膨張弁と膨張弁バイパス手段とを切り換える手段とを含
み、冷媒循環系を蒸気圧縮冷凍サイクルと自然循環ルー
プとに切り換え可能な冷房装置において、 前記冷媒液の流路に接続され、前記冷媒液を溜めて前記
凝縮器内部の冷媒液面の滞留を除去する冷媒液溜めを有
することを特徴とする冷房装置。2. An evaporator which absorbs heat of vaporization when a refrigerant liquid becomes a refrigerant gas from a cooled portion, a gas pipe which is connected to the evaporator and raises the refrigerant gas, and which is connected to the gas pipe and thereby A condenser that liquefies the introduced refrigerant gas into a refrigerant liquid, a liquid pipe that is connected to this condenser and that guides the refrigerant liquid generated by this to the evaporator by descending by gravity, and the middle of the gas pipe A compressor for adiabatically compressing the refrigerant gas, a compressor bypass means for bypassing the compressor, a means for switching between the compressor and the compressor bypass means, and a refrigerant liquid inserted in the liquid pipe to reduce the pressure of the refrigerant liquid. Expansion valve and expansion valve bypass means for bypassing the expansion valve,
In a cooling device that includes a means for switching between an expansion valve and an expansion valve bypass means and is capable of switching the refrigerant circulation system between a vapor compression refrigeration cycle and a natural circulation loop, the refrigerant liquid being connected to the flow path of the refrigerant liquid, A cooling device having a refrigerant liquid reservoir for accumulating and removing retention of the liquid surface of the refrigerant inside the condenser.
において、 前記冷媒液溜めは、前記凝縮器への前記液配管の接続位
置の高さに設けられることを特徴とする冷房装置。3. The cooling device according to claim 1 or 2, wherein the refrigerant liquid reservoir is provided at a height of a connection position of the liquid pipe to the condenser.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8084889A JPH09273876A (en) | 1996-04-08 | 1996-04-08 | Cooler with natural circulation loop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8084889A JPH09273876A (en) | 1996-04-08 | 1996-04-08 | Cooler with natural circulation loop |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09273876A true JPH09273876A (en) | 1997-10-21 |
Family
ID=13843331
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8084889A Pending JPH09273876A (en) | 1996-04-08 | 1996-04-08 | Cooler with natural circulation loop |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09273876A (en) |
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|---|---|---|---|---|
| US6442959B1 (en) | 2000-06-28 | 2002-09-03 | Twinbird Corporation | Thermosiphon for refrigerating machine |
| JP2003148838A (en) * | 2001-11-09 | 2003-05-21 | Mitsubishi Electric Corp | Air conditioner, refrigeration cycle device, refrigerant charging method |
| JP2008096084A (en) * | 2006-10-16 | 2008-04-24 | Hoshizaki Electric Co Ltd | Thermosiphon |
| JP2008096085A (en) * | 2006-10-16 | 2008-04-24 | Hoshizaki Electric Co Ltd | Cooling apparatus |
| JP2011069546A (en) * | 2009-09-25 | 2011-04-07 | Fujitsu Ltd | Loop type heat pipe and electronic equipment |
| JP2011089660A (en) * | 2009-10-20 | 2011-05-06 | Chubu Electric Power Co Inc | Superconductive magnet incorporating self-excited oscillation type heat pipe |
| WO2012081110A1 (en) * | 2010-12-16 | 2012-06-21 | 株式会社 日立製作所 | Air-conditioner |
| JP2012129408A (en) * | 2010-12-16 | 2012-07-05 | Hitachi Ltd | Cooling system for data center |
| EP2188576A4 (en) * | 2007-09-18 | 2013-12-18 | Carrier Corp | METHODS AND SYSTEMS FOR CONTROLLING INTEGRATED AIR CONDITIONING SYSTEMS |
| KR101462126B1 (en) * | 2014-07-08 | 2014-11-14 | 주식회사 주원엔지니어링 | Split heat transfer heat-pipe system |
| JP2015210011A (en) * | 2014-04-25 | 2015-11-24 | 株式会社ササクラ | Natural circulation cooling system |
| JP2016507043A (en) * | 2013-02-14 | 2016-03-07 | ユーロ ヒート パイプス | Heat transport device using two-phase fluid |
| JP2016080300A (en) * | 2014-10-21 | 2016-05-16 | Gac株式会社 | Cooling unit and cooling system |
| JP2016164478A (en) * | 2015-03-06 | 2016-09-08 | 株式会社東芝 | Cooling system |
| DE102015206478A1 (en) * | 2015-04-10 | 2016-10-13 | Wobben Properties Gmbh | Wind turbine with liquid circuit and components for it |
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|---|---|---|---|---|
| US6442959B1 (en) | 2000-06-28 | 2002-09-03 | Twinbird Corporation | Thermosiphon for refrigerating machine |
| JP2003148838A (en) * | 2001-11-09 | 2003-05-21 | Mitsubishi Electric Corp | Air conditioner, refrigeration cycle device, refrigerant charging method |
| JP2008096084A (en) * | 2006-10-16 | 2008-04-24 | Hoshizaki Electric Co Ltd | Thermosiphon |
| JP2008096085A (en) * | 2006-10-16 | 2008-04-24 | Hoshizaki Electric Co Ltd | Cooling apparatus |
| EP2188576A4 (en) * | 2007-09-18 | 2013-12-18 | Carrier Corp | METHODS AND SYSTEMS FOR CONTROLLING INTEGRATED AIR CONDITIONING SYSTEMS |
| US9909790B2 (en) | 2007-09-18 | 2018-03-06 | Carrier Corporation | Methods and systems for controlling integrated air conditioning systems |
| US11761686B2 (en) | 2007-09-18 | 2023-09-19 | Carrier Corporation | Methods and systems for controlling integrated air conditioning systems |
| JP2011069546A (en) * | 2009-09-25 | 2011-04-07 | Fujitsu Ltd | Loop type heat pipe and electronic equipment |
| JP2011089660A (en) * | 2009-10-20 | 2011-05-06 | Chubu Electric Power Co Inc | Superconductive magnet incorporating self-excited oscillation type heat pipe |
| JP2012129408A (en) * | 2010-12-16 | 2012-07-05 | Hitachi Ltd | Cooling system for data center |
| JPWO2012081110A1 (en) * | 2010-12-16 | 2014-05-22 | 株式会社日立製作所 | Air conditioner |
| WO2012081110A1 (en) * | 2010-12-16 | 2012-06-21 | 株式会社 日立製作所 | Air-conditioner |
| JP2016507043A (en) * | 2013-02-14 | 2016-03-07 | ユーロ ヒート パイプス | Heat transport device using two-phase fluid |
| US10234213B2 (en) | 2013-02-14 | 2019-03-19 | Euro Heat Pipes | Device for heat transport with two-phase fluid |
| JP2015210011A (en) * | 2014-04-25 | 2015-11-24 | 株式会社ササクラ | Natural circulation cooling system |
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| JP2016080300A (en) * | 2014-10-21 | 2016-05-16 | Gac株式会社 | Cooling unit and cooling system |
| JP2016164478A (en) * | 2015-03-06 | 2016-09-08 | 株式会社東芝 | Cooling system |
| US10845127B2 (en) | 2015-03-06 | 2020-11-24 | Kabushiki Kaisha Toshiba | Cooling device |
| WO2016143213A1 (en) * | 2015-03-06 | 2016-09-15 | 株式会社東芝 | Cooling device |
| WO2016162457A1 (en) | 2015-04-10 | 2016-10-13 | Wobben Properties Gmbh | Wind turbine having a liquid circuit and components therefor |
| JP2018510996A (en) * | 2015-04-10 | 2018-04-19 | ヴォッベン プロパティーズ ゲーエムベーハーWobben Properties Gmbh | Wind power generator having fluid circuit and components therefor |
| DE102015206478A1 (en) * | 2015-04-10 | 2016-10-13 | Wobben Properties Gmbh | Wind turbine with liquid circuit and components for it |
| US10626853B2 (en) | 2015-04-10 | 2020-04-21 | Wobben Properties Gmbh | Wind turbine having a liquid circuit and components therefore |
| CN112764301A (en) * | 2019-11-05 | 2021-05-07 | 青岛海信激光显示股份有限公司 | Light processing projector |
| CN112782915A (en) * | 2019-11-05 | 2021-05-11 | 青岛海信激光显示股份有限公司 | Light processing projector |
| CN112782915B (en) * | 2019-11-05 | 2024-08-02 | 青岛海信激光显示股份有限公司 | Light processing projector |
| CN111964188A (en) * | 2020-08-25 | 2020-11-20 | 南京工业大学 | Thermosiphon-vapor compression composite refrigeration system |
| CN111964188B (en) * | 2020-08-25 | 2022-03-08 | 南京工业大学 | Thermosiphon-vapor compression composite refrigeration system |
| CN113720041A (en) * | 2021-08-06 | 2021-11-30 | 陈洪涛 | Heat pump unit and energy-saving heat pump system |
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