JPH0486433A - Cooling device and cooling/heating device - Google Patents
Cooling device and cooling/heating deviceInfo
- Publication number
- JPH0486433A JPH0486433A JP20314890A JP20314890A JPH0486433A JP H0486433 A JPH0486433 A JP H0486433A JP 20314890 A JP20314890 A JP 20314890A JP 20314890 A JP20314890 A JP 20314890A JP H0486433 A JPH0486433 A JP H0486433A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- condenser
- gas
- refrigerant
- tank
- 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
- 238000001816 cooling Methods 0.000 title claims description 31
- 238000010438 heat treatment Methods 0.000 title claims description 9
- 239000007788 liquid Substances 0.000 claims abstract description 132
- 239000003507 refrigerant Substances 0.000 claims abstract description 58
- 238000004378 air conditioning Methods 0.000 claims description 16
- 239000007791 liquid phase Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 abstract 1
- 230000005494 condensation Effects 0.000 description 7
- 238000009833 condensation Methods 0.000 description 7
- 238000000926 separation method Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、冷房装置および冷暖房装置に係わり、特に、
気液相変化する冷媒を用いた冷房装置および冷暖房装置
に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a cooling device and a heating and cooling device, and in particular,
The present invention relates to a cooling device and an air-conditioning device using a refrigerant that changes gas-liquid phase.
従来、フロン系冷媒のように気液相変化する冷媒を用い
た冷暖房装置としては、例えば、本出願人が先に出願し
た特開平2−57835号公報に開示されるものが知ら
れている。BACKGROUND ART Conventionally, as a heating and cooling apparatus using a refrigerant that undergoes a gas-liquid phase change, such as a fluorocarbon-based refrigerant, there is known, for example, the one disclosed in Japanese Patent Laid-Open No. 2-57835, which was previously filed by the present applicant.
第3図は、この公報に開示される冷暖房装置を示すもの
で、この冷暖房装置は、受液タンク11と、外部からの
冷、温熱源と熱交換する凝縮器兼蒸発器13と、室内空
気と熱交換する、少なくとも一白以上の室側蒸発器兼凝
縮器15と、所要の配管および冷暖切換弁と、これ等に
より熱サイクルを行なわせる液ポンプ17とを配設して
構成され、さらに、熱運搬手段としてフロン系冷媒が使
用されている。FIG. 3 shows the air conditioning system disclosed in this publication. It is composed of an indoor evaporator/condenser 15 of at least one size or more, which exchanges heat with the indoor evaporator/condenser 15, necessary piping and cooling/heating switching valves, and a liquid pump 17 that performs a heat cycle using these. , Freon-based refrigerants are used as heat transport means.
以上のような冷暖房装置では、熱運搬手段としてフロン
系冷媒を循環使用するようにしたので、冷媒の搬送量が
少なくなり、動力が低減されるとともに、配管のサイズ
を縮小し、配設スペースを節約することが可能となる。In the above-mentioned air-conditioning equipment, a fluorocarbon-based refrigerant is circulated as a heat transport means, which reduces the amount of refrigerant transported, reduces power consumption, and reduces the size of piping to save installation space. It becomes possible to save money.
また、従来の液ポンプ方式では、冷房しか行なうことが
できないが、この冷暖房装置では、可逆サイクルのため
、冷、暖両用に利用でき、さらに、D HC熱源使用に
も適し、また、室内の負荷のアンバランスに対しても容
易に制御可能である。In addition, while conventional liquid pump systems can only perform cooling, this air-conditioning system has a reversible cycle, so it can be used for both cooling and heating purposes, and is also suitable for use as a DHC heat source. It is also possible to easily control the imbalance.
そして、この冷暖房装置では、冷房時には、液ポンプ1
7が作動され、受液タンク11内の冷媒は、図に太線で
示すように、第1管路18を通り室側蒸発器兼凝縮器1
5に流入し、ここで蒸発作用を受は室内側の空気を冷房
し、この後、第2管路19を通って蒸発器兼凝縮器13
に流入し、ここで凝縮作用を受け、第3管路20を通っ
て受液タンク11内に循環する。In this air-conditioning system, during cooling, the liquid pump 1
7 is activated, and the refrigerant in the liquid receiving tank 11 passes through the first pipe line 18 to the indoor evaporator/condenser 1, as shown by the thick line in the figure.
The air flows into the evaporator/condenser 13 through the second pipe line 19, where it receives the evaporative action and cools the indoor air.
The liquid flows into the liquid receiving tank 11, undergoes a condensation action there, and circulates through the third pipe line 20 into the liquid receiving tank 11.
しかしながら、このような従来の冷暖房装置では、冷房
時に、室側蒸発器兼凝縮器15の熱交換効率を向上する
ために、液ポンプ17により、室側蒸発器兼凝縮器15
に多量の液状の冷媒を供給すると、液状の冷媒の一部が
そのまま第2管路19に流入し、第2管路19内の冷媒
は、ガス分と液分とが混合した状態になり、この状態の
冷媒を凝縮器兼蒸発器13にそのまま導くと、凝縮器兼
蒸発器13における凝縮効率が極端に低下するという問
題があった。However, in such a conventional air conditioning system, in order to improve the heat exchange efficiency of the indoor evaporator/condenser 15 during cooling, the liquid pump 17 is used to increase the heat exchange efficiency of the indoor evaporator/condenser 15.
When a large amount of liquid refrigerant is supplied to the refrigerant, a part of the liquid refrigerant flows directly into the second pipe line 19, and the refrigerant in the second pipe line 19 becomes a mixture of gas and liquid parts. If the refrigerant in this state is directly led to the condenser/evaporator 13, there is a problem in that the condensation efficiency in the condenser/evaporator 13 is extremely reduced.
本発明は、上記のような問題を解決したもので、凝縮器
における凝縮効率を従来より大幅に向上することのでき
る冷房装置および冷暖房装置を提供することを目的とす
る。The present invention solves the above-mentioned problems, and aims to provide a cooling device and an air-conditioning device that can significantly improve the condensing efficiency of a condenser compared to the conventional one.
〔課題を解決するための手段]
本発明にかかわる冷房装置は、気液相変化する冷媒を液
体状態で収容する受液タンクと、前記冷媒と室内空気と
を熱交換させる蒸発器と、前記冷媒と外部からの冷熱源
とを熱交換させる凝縮器と、前記受液タンクの出口側と
前記蒸発器の一側とを接続し液ポンプの介装される第1
管路と、前記蒸発器の他側と前記凝縮器の一側とを接続
する第2管路と、前記凝縮器の他側と受液タンクの入口
側とを接続する第3管路とを備えた冷房装置において、
前記第2管路に、第2管路内のガス分と液分との分離を
行ないガス分のみを凝縮器に導く気液分離装置を配置す
るとともに、この気液分離装置を、前記受液タンクの上
方に配置され、分断された前記第2管路の一対の分断端
部が上部のガス部に開口されるタンク本体と、このタン
ク本体の下部開口と受液タンクの上部のガス部とを接続
するドレン管路とから構成し、このドレン管路の一部を
、前記タンク本体内の冷媒の最大液位面まで、上方に向
けて突出し液位調整部を形成してなるものである。[Means for Solving the Problems] A cooling device according to the present invention includes: a liquid receiving tank that stores a refrigerant that undergoes a gas-liquid phase change in a liquid state; an evaporator that exchanges heat between the refrigerant and indoor air; a condenser that exchanges heat between the liquid receiving tank and a cold source from the outside; a first liquid pump that connects the outlet side of the liquid receiving tank and one side of the evaporator and is equipped with a liquid pump;
a pipe line, a second pipe line connecting the other side of the evaporator and one side of the condenser, and a third pipe line connecting the other side of the condenser and the inlet side of the liquid receiving tank. In the cooling device equipped with
A gas-liquid separator is disposed in the second pipe line to separate gas and liquid in the second pipe line and guide only the gas content to the condenser, and this gas-liquid separator is connected to the liquid receiving liquid. a tank body disposed above the tank, in which a pair of divided ends of the second pipe line are opened to an upper gas section; a lower opening of the tank body and an upper gas section of the liquid receiving tank; and a drain pipe connecting the refrigerant, and a part of the drain pipe protrudes upward to the maximum liquid level of the refrigerant in the tank body to form a liquid level adjustment part. be.
本発明の冷暖房装置は、気液相変化する冷媒を液体状態
で収容する受液タンクと、前記冷媒と室内空気とを熱交
換させる蒸発器と、前記冷媒と外部からの冷熱源とを熱
交換させる凝縮器と、前記受液タンクの出口側と前記蒸
発器の一側とを接続し液ポンプの介装される第1管路と
、前記蒸発器の他側と前記凝縮器の一例とを接続する第
2管路と、前記凝縮器の他側と受液タンクの入口側とを
接続する第3管路とを備えた冷房回路を有する冷暖房装
置において、前記第2管路に、第2管路内のガス分と液
分との分離を行ないガス分のみを凝縮器に導く気液分離
装置を配置するとともに、この気液分離装置を、前記受
液タンクの上方に配置され、分断された前記第2管路の
一対の分断端部が上部のガス部に開口されるタンク本体
と、このタンク本体の下部開口と受液タンクの上部のガ
ス部とを接続するドレン管路とから構成し、このドレン
管路の一部を、前記タンク本体内の冷媒の最大液位面ま
で、上方に向けて突出し液位調整部を形成してなるもの
である。The air conditioning system of the present invention includes a liquid receiving tank that stores a refrigerant that undergoes a gas-liquid phase change in a liquid state, an evaporator that exchanges heat between the refrigerant and indoor air, and an external cooling source that exchanges heat with the refrigerant. a first pipe line connecting the outlet side of the liquid receiving tank and one side of the evaporator and having a liquid pump interposed therein; and an example of the condenser connecting the other side of the evaporator with In the air-conditioning device, the cooling/heating system has a cooling circuit including a second conduit connecting the condenser, and a third conduit connecting the other side of the condenser and the inlet side of the liquid receiving tank. A gas-liquid separator that separates gas and liquid in the pipe line and guides only the gas to the condenser is disposed, and this gas-liquid separator is disposed above the liquid receiving tank and separated. A tank body in which the pair of divided ends of the second pipe line are opened to the upper gas part, and a drain pipe connecting the lower opening of the tank body and the upper gas part of the liquid receiving tank. A part of the drain pipe is protruded upward to the maximum liquid level of the refrigerant in the tank body to form a liquid level adjustment part.
(作 用〕
本発明の冷房装置および冷暖房装置においては、冷房時
には、受液タンク内の冷媒は、第1管路を通り蒸発器に
流入し、ここで蒸発作用を受は室内側の空気を冷房し、
第2管路を通って凝縮器に流入し、ここで凝縮作用を受
け、この後、第3管路を通って受液タンク内に循環する
。(Function) In the cooling device and air conditioning device of the present invention, during cooling, the refrigerant in the liquid receiving tank flows into the evaporator through the first pipe, where it undergoes an evaporative action and absorbs indoor air. Air conditioned,
It enters the condenser through the second line, where it is subjected to condensation action, and is then circulated through the third line into the receiving tank.
そして、本発明では、第2管路に配置される気液分離装
置により、第2管路内のガス分と液分との分離が行なわ
れ、ガス分のみが凝縮器に導かれる。In the present invention, the gas-liquid separator disposed in the second pipe separates the gas and liquid in the second pipe, and only the gas is guided to the condenser.
すなわち、第2管路内のガス分と液分とを含んだ冷媒は
、蒸発器側の分断端部からタンク本体の上部に流出され
、軽いガス分のみが、凝縮器側の分断端部から凝縮器に
導かれ凝縮器において凝縮される。That is, the refrigerant containing gas and liquid in the second pipe flows out from the divided end on the evaporator side to the upper part of the tank body, and only the light gas component flows out from the divided end on the condenser side. It is led from the part to the condenser and condensed in the condenser.
一方、タンク本体内に流入した液分が所定の液位を越え
ると、冷媒が、ドレン管路に形成される液位調整部を越
えて受液タンク側に導かれる。On the other hand, when the liquid that has flowed into the tank body exceeds a predetermined liquid level, the refrigerant is guided to the liquid receiving tank side beyond a liquid level adjustment part formed in the drain pipe.
以下、本発明の詳細を図面に示す実施例について説明す
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, details of the present invention will be described with reference to embodiments shown in the drawings.
第1図は、本発明の冷房装置の一実施例を示すもので、
図において符号21は、例えば、フロン系冷媒のように
気液相変化する冷媒を液体状態で収容する受液タンクを
示している。FIG. 1 shows an embodiment of the cooling device of the present invention.
In the figure, the reference numeral 21 indicates a liquid receiving tank that stores a refrigerant that undergoes a gas-liquid phase change, such as a fluorocarbon refrigerant, in a liquid state.
符号23は、冷媒と室内空気とを熱交換させる複数台の
蒸発器(1台のみを図示)を示している。Reference numeral 23 indicates a plurality of evaporators (only one is shown) that exchange heat between the refrigerant and indoor air.
符号25は、冷媒と外部からの冷熱源とを熱交換させる
凝縮器を示しており、この凝縮器25には、外部から冷
水等の冷熱源を供給するための冷熱源供給配管27が挿
通されている。Reference numeral 25 indicates a condenser for exchanging heat between the refrigerant and a cold source from the outside, and a cold source supply pipe 27 for supplying a cold source such as cold water from the outside is inserted through the condenser 25. ing.
受液タンク21の出口側と蒸発器23の一側とを接続し
て第1管路29が形成されており、この第1管路29に
は、液ポンプ31が配置されている。A first pipe line 29 is formed by connecting the outlet side of the liquid receiving tank 21 and one side of the evaporator 23, and a liquid pump 31 is arranged in this first pipe line 29.
また、蒸発器23の他側と凝縮器25の一側とを接続し
て第2管路33が形成されている。Further, a second pipe line 33 is formed by connecting the other side of the evaporator 23 and one side of the condenser 25.
さらに、凝縮器25の他側と受液タンク21の入口側と
を接続して第3管路35が形成されている。Furthermore, a third pipe line 35 is formed by connecting the other side of the condenser 25 and the inlet side of the liquid receiving tank 21.
そして、この実施例では、第2管路33には、第2管路
33内のガス分と液分との分離を行ないガス分のみを凝
縮器25に導く気液分離装置37が配置されている。In this embodiment, a gas-liquid separator 37 is arranged in the second pipe line 33 to separate the gas and liquid parts in the second pipe line 33 and guide only the gas part to the condenser 25. There is.
この気液分離装置37は、受液タンク21の上方に配置
されるタンク本体39を有している。This gas-liquid separation device 37 has a tank body 39 disposed above the liquid receiving tank 21 .
このタンク本体39の上部のガス部38には、分断され
た第2管路33の一対の分断端部41゜43が開口され
ている。A pair of divided ends 41° and 43 of the divided second pipe line 33 are opened in the upper gas section 38 of the tank body 39.
タンク本体39の下部開口と受液タンク21の上部のガ
ス部49とを接続してドレン管路45が配置されている
。A drain pipe 45 is arranged to connect the lower opening of the tank body 39 and the upper gas section 49 of the liquid receiving tank 21 .
そして、このドレン管路45の一部が、タンク本体39
内の冷媒の最大液位面りまで、上方に向けて突出され、
液位調整部47が形成されている。A part of this drain pipe 45 is connected to the tank body 39.
It is projected upward to the maximum liquid level of the refrigerant inside.
A liquid level adjustment section 47 is formed.
以上のように構成された冷房装置では、液ポンプ31が
作動されると、受液タンク21内の冷媒は、第1管路2
9を通り蒸発器23に流入し、ここで蒸発作用を受は室
内側の空気を冷房し、第2管路33を通って凝縮器25
に流入し、ここで凝縮作用を受け、この後、第3管路3
5を通って受液タンク21内に循環する。In the cooling device configured as described above, when the liquid pump 31 is operated, the refrigerant in the liquid receiving tank 21 is transferred to the first pipe line 2.
9, the air flows into the evaporator 23, where it receives an evaporative action, cools the indoor air, and flows through the second pipe line 33 to the condenser 25.
, where it is condensed, and then flows into the third pipe 3.
5 and circulates into the liquid receiving tank 21.
しかして、以上のように構成された冷房装置では、第2
管路33に、第2管路33内のガス分と液分との分離を
行ないガス分のみを凝縮器25に導く気液分離装置37
を配置するとともに、この気液分離装置37を、受液タ
ンク21の上方に配置され、分断された第2管路33の
一対の分断端部41,43が上部のガス部に開口される
タンク本体39と、このタンク本体39の下部開口と受
液タンク21の上部のガス部49とを接続するドレン管
路45とから構成し、このドレン管路45の一部を、タ
ンク本体39内の冷媒の最大液位面りまで、上方に向け
て突出し液位調整部47を形成したので、第2管路33
内のガス分と液分とを含んだ冷媒は、蒸発器23例の分
断端部41からタンク本体39の上部に流出され、軽い
ガス分のみが、凝縮器25例の分断端部43から凝縮器
25に導かれ凝縮器25において凝縮され、一方、タン
ク本体39内に流入した液分は、タンク本体39内に流
入した液分が所定の液位を越えると、冷媒が、ドレン管
路45に形成される液位調整部47を越えて受液タンク
21側に導かれるため、凝縮器25に供給される冷媒に
は、凝縮の不要な熱交換効率を低下させる液状の冷媒が
含まれることがなく、凝縮器25における凝縮効率を従
来より大幅に向上することが可能となる。However, in the cooling device configured as above, the second
A gas-liquid separation device 37 is provided in the pipe 33 to separate the gas and liquid in the second pipe 33 and guide only the gas to the condenser 25.
At the same time, this gas-liquid separation device 37 is arranged above the liquid receiving tank 21, and the pair of divided ends 41 and 43 of the divided second pipe line 33 are opened to the upper gas section. It consists of a tank body 39 and a drain pipe 45 that connects the lower opening of the tank body 39 and the upper gas section 49 of the liquid receiving tank 21. Since the liquid level adjustment part 47 is formed to protrude upward to the maximum liquid level of the refrigerant, the second pipe line 33
The refrigerant containing gas and liquid in the tank is discharged from the divided end 41 of the 23 evaporators to the upper part of the tank body 39, and only the light gas is discharged from the divided end 43 of the 25 condensers. The refrigerant is led to the condenser 25 and condensed in the condenser 25. On the other hand, when the liquid that has flowed into the tank body 39 exceeds a predetermined liquid level, the refrigerant flows into the drain pipe. Since the refrigerant is guided to the liquid receiving tank 21 side beyond the liquid level adjustment part 47 formed in the passage 45, the refrigerant supplied to the condenser 25 contains liquid refrigerant that does not require condensation and reduces heat exchange efficiency. Therefore, the condensation efficiency in the condenser 25 can be significantly improved compared to the conventional case.
また、以上のように構成された冷房装置では、ドレン管
路45の一部を、タンク本体39内の冷媒の最大液位面
りまで、上方に向けて突出し液位調整部47を形成した
ので、制御弁、センサー等の特別な装置を必要とするこ
となく、容易確実に液位の調節を行なうことが可能とな
る。Further, in the cooling device configured as described above, a part of the drain pipe 45 is formed to protrude upward to the maximum liquid level of the refrigerant in the tank body 39 to form the liquid level adjustment part 47. It becomes possible to easily and reliably adjust the liquid level without requiring any special equipment such as a control valve or sensor.
第2図は、本発明の冷暖房装置の一実施例を示すもので
、この実施例では、室内には、蒸発器と凝縮器との機能
を備えた室側蒸発器兼凝縮器51が配置され、また、室
外には、冷媒と外部からの温熱源とを熱交換させる蒸発
器53が配置されている。FIG. 2 shows an embodiment of the air conditioning system of the present invention. In this embodiment, an indoor evaporator/condenser 51 having the functions of an evaporator and a condenser is arranged indoors. Also, an evaporator 53 is arranged outside the room to exchange heat between the refrigerant and a heat source from the outside.
この蒸発器53には、外部から温水等の温熱源を供給す
るための温熱源供給配管55が挿通されている。A heat source supply pipe 55 for supplying a heat source such as hot water from the outside is inserted into the evaporator 53 .
受液タンク21の出口側と蒸発器53の一例とを接続し
て第4管路57が形成されており、この第4管路57に
は、開閉弁59が配置されている。A fourth pipe line 57 is formed by connecting the outlet side of the liquid receiving tank 21 and an example of the evaporator 53, and an on-off valve 59 is disposed in the fourth pipe line 57.
また、蒸発器53の他側と室側蒸発器兼凝縮器51の他
側とを接続して第5管路61が形成されている。Further, a fifth pipe line 61 is formed by connecting the other side of the evaporator 53 and the other side of the indoor evaporator/condenser 51.
さらに、第1管路29の開閉弁63と室側蒸発器兼凝縮
器51との間から分岐して、受液タンク21の入口側に
接続する第6管路65が配置されており、この第6管路
65には、開閉弁67が配置されている。Furthermore, a sixth pipe line 65 is arranged which branches from between the on-off valve 63 of the first pipe line 29 and the indoor evaporator/condenser 51 and connects to the inlet side of the liquid receiving tank 21. An on-off valve 67 is arranged in the sixth conduit 65.
そして、第2管路33には、上述した実施例の気液分離
装置37と同一の気液分離装置が配置されている。In the second pipe line 33, a gas-liquid separation device that is the same as the gas-liquid separation device 37 of the above-described embodiment is arranged.
以上のように構成された冷暖房装置では、冷房は、室側
蒸発器兼凝縮器51を蒸発器として使用し、前述した実
施例とほぼ同様に行なわれる。In the air-conditioning system configured as described above, cooling is performed using the indoor evaporator/condenser 51 as an evaporator in substantially the same manner as in the embodiment described above.
一方、暖房は、液ポンプ31の作動により、受液タンク
21内の冷媒を、第4管路57を通り蒸発器53に流入
させ、ここで蒸発作用を受けた冷媒を、第5管路61を
通して室側蒸発器兼凝縮器51に流入させ、ここで凝縮
作用を受は室内側の空気を暖房した冷媒を、第6管路6
5を通して受液タンク21内に循環することにより行な
われる。On the other hand, for heating, the liquid pump 31 is operated to cause the refrigerant in the liquid receiving tank 21 to flow into the evaporator 53 through the fourth pipe line 57, and the refrigerant subjected to evaporation here is transferred to the fifth pipe line 61. The refrigerant that heated the indoor air is flowed into the indoor evaporator/condenser 51 where it is condensed.
This is done by circulating the liquid through the liquid receiving tank 21 through the liquid receiving tank 21.
以上のように構成された冷暖房装置においても、冷房時
には、第1図に示した実施例とほぼ同様の効果を得るこ
とができる。Even in the air-conditioning device configured as described above, substantially the same effect as the embodiment shown in FIG. 1 can be obtained during cooling.
以上述べたように、本発明によれば、第2管路に、第2
管路内のガス分と液分との分離を行ないガス分のみを凝
縮器に導く気液分離装置を配置するとともに、この気液
分離装置を、受液タンクの上方に配置され、分断された
第2管路の一対の分断端部が上部のガス部に開口される
タンク本体と、このタンク本体の下部開口と受液タンク
の上部のガス部とを接続するドレン管路とから構成し、
このドレン管路の一部を、タンク本体内の冷媒の最大液
位面まで、上方に向けて突出し液位調整部を形成したの
で、第2管路内のガス分と液分とを含んだ冷媒は、蒸発
器側の分断端部からタンク本体の上部に流出され、軽い
ガス分のみが、凝縮器側の分断端部から凝縮器に導かれ
凝縮器において凝縮され、一方、タンク本体内に流入し
た液分は、所定の液位を越えると、冷媒が、ドレン管路
に形成される液位調整部を越えて受液タンク側に導かれ
るため、凝縮器に供給される冷媒には、凝縮の不要な熱
交換効率を低下させる液状の冷媒が含まれることがなく
、凝縮器における凝縮効率を従来より大幅に向上するこ
とができるという利点がある。As described above, according to the present invention, the second
A gas-liquid separator is installed that separates the gas and liquid in the pipeline and guides only the gas to the condenser.This gas-liquid separator is placed above the liquid receiving tank and It consists of a tank main body in which a pair of divided ends of the second pipe are opened to the upper gas section, and a drain pipe connecting the lower opening of the tank main body and the upper gas section of the liquid receiving tank. ,
A part of this drain pipe was formed to protrude upward to the maximum liquid level of the refrigerant in the tank body to form a liquid level adjustment part, so that the liquid level contained in the second pipe was contained. The refrigerant flows out from the divided end on the evaporator side to the upper part of the tank body, and only the light gas component is led to the condenser from the divided end on the condenser side and is condensed in the condenser. When the liquid that has flowed into the tank exceeds a predetermined level, the refrigerant is guided to the liquid receiving tank beyond the liquid level adjustment part formed in the drain pipe, so that the refrigerant supplied to the condenser is This has the advantage that it does not contain a liquid refrigerant that reduces heat exchange efficiency and does not require condensation, and the condensation efficiency in the condenser can be significantly improved compared to the conventional method.
第1図は本発明の冷房装置の一実施例を示す配管系統図
である。
第2図は本発明の冷暖房装置の一実施例を示す配管系統
図である。
第3図は従来の冷暖房装置を示す配管系統図である。
〔主要な部分の符号の説明〕
21・・ ・受液タンク
23・・・蒸発器
25・・・凝縮器
29・・・第1管路
31・・・液ポンプ
33・・・第2管路
35・・・第3管路
38.49・・・ガス部
39・・・タンク本体
41.43・・・分断端部
45・・・ドレン管路
47・・・液位調整部。
第1図
第 3 図FIG. 1 is a piping system diagram showing an embodiment of the cooling device of the present invention. FIG. 2 is a piping system diagram showing an embodiment of the air conditioning system of the present invention. FIG. 3 is a piping system diagram showing a conventional heating and cooling system. [Explanation of symbols of main parts] 21... ・Liquid receiving tank 23...Evaporator 25...Condenser 29...First pipe line 31...Liquid pump 33...Second pipe line 35...Third pipe line 38.49...Gas section 39...Tank body 41.43...Divided end portion 45...Drain pipe line 47...Liquid level adjustment part. Figure 1 Figure 3
Claims (2)
ンクと、前記冷媒と室内空気とを熱交換させる蒸発器と
、前記冷媒と外部からの冷熱源とを熱交換させる凝縮器
と、前記受液タンクの出口側と前記蒸発器の一側とを接
続し液ポンプの介装される第1管路と、前記蒸発器の他
側と前記凝縮器の一側とを接続する第2管路と、前記凝
縮器の他側と受液タンクの入口側とを接続する第3管路
とを備えた冷房装置において、前記第2管路に、第2管
路内のガス分と液分との分離を行ないガス分のみを凝縮
器に導く気液分離装置を配置するとともに、この気液分
離装置を、前記受液タンクの上方に配置され、分断され
た前記第2管路の一対の分断端部が上部のガス部に開口
されるタンク本体と、このタンク本体の下部開口と受液
タンクの上部のガス部とを接続するドレン管路とから構
成し、このドレン管路の一部を、前記タンク本体内の冷
媒の最大液位面まで、上方に向けて突出し液位調整部を
形成してなることを特徴とする冷房装置。(1) A liquid receiving tank that stores a refrigerant that changes gas-liquid phase in a liquid state, an evaporator that exchanges heat between the refrigerant and indoor air, and a condenser that exchanges heat between the refrigerant and an external cold source. , a first pipe line connecting the outlet side of the liquid receiving tank and one side of the evaporator and having a liquid pump interposed therein; and a first pipe line connecting the other side of the evaporator and one side of the condenser. In the cooling device comprising two pipes and a third pipe connecting the other side of the condenser and the inlet side of the liquid receiving tank, the second pipe is connected to the gas in the second pipe. A gas-liquid separator is disposed that separates the gas from the liquid and leads only the gas to the condenser, and this gas-liquid separator is disposed above the liquid receiving tank and connected to the separated second pipe It consists of a tank body with a pair of divided ends opening into the upper gas section, and a drain pipe connecting the lower opening of the tank main body and the upper gas part of the liquid receiving tank. A cooling device characterized in that a part of the tank body is formed by protruding upward to a maximum liquid level of the refrigerant in the tank body to form a liquid level adjustment part.
ンクと、前記冷媒と室内空気とを熱交換させる蒸発器と
、前記冷媒と外部からの冷熱源とを熱交換させる凝縮器
と、前記受液タンクの出口側と前記蒸発器の一側とを接
続し液ポンプの介装される第1管路と、前記蒸発器の他
側と前記凝縮器の一側とを接続する第2管路と、前記凝
縮器の他側と受液タンクの入口側とを接続する第3管路
とを備えた冷房回路を有する冷暖房装置において、前記
第2管路に、第2管路内のガス分と液分との分離を行な
いガス分のみを凝縮器に導く気液分離装置を配置すると
ともに、この気液分離装置を、前記受液タンクの上方に
配置され、分断された前記第2管路の一対の分断端部が
上部のガス部に開口されるタンク本体と、このタンク本
体の下部開口と受液タンクの上部のガス部とを接続する
ドレン管路とから構成し、このドレン管路の一部を、前
記タンク本体内の冷媒の最大液位面まで、上方に向けて
突出し液位調整部を形成してなることを特徴とする冷暖
房装置。(2) A liquid receiving tank that stores a refrigerant that changes in gas-liquid phase in a liquid state, an evaporator that exchanges heat between the refrigerant and indoor air, and a condenser that exchanges heat between the refrigerant and an external cold source. , a first pipe line connecting the outlet side of the liquid receiving tank and one side of the evaporator and having a liquid pump interposed therein; and a first pipe line connecting the other side of the evaporator and one side of the condenser. In the air conditioning system, the air conditioning system has a cooling circuit including two pipes and a third pipe connecting the other side of the condenser and the inlet side of the liquid receiving tank. A gas-liquid separator is disposed that separates the gas component from the liquid component and guides only the gas component to the condenser, and the gas-liquid separator is disposed above the liquid receiving tank and Consisting of a tank body in which a pair of divided ends of two pipes are opened to the upper gas part, and a drain pipe connecting the lower opening of the tank body and the upper gas part of the liquid receiving tank, A heating and cooling device characterized in that a part of the drain pipe is protruded upward to a maximum liquid level of the refrigerant in the tank body to form a liquid level adjustment part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20314890A JP2859718B2 (en) | 1990-07-31 | 1990-07-31 | Cooling and cooling systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20314890A JP2859718B2 (en) | 1990-07-31 | 1990-07-31 | Cooling and cooling systems |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0486433A true JPH0486433A (en) | 1992-03-19 |
| JP2859718B2 JP2859718B2 (en) | 1999-02-24 |
Family
ID=16469222
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20314890A Expired - Lifetime JP2859718B2 (en) | 1990-07-31 | 1990-07-31 | Cooling and cooling systems |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2859718B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111023271A (en) * | 2019-12-31 | 2020-04-17 | 宁波奥克斯电气股份有限公司 | Adjustment device, system and control method of multi-line refrigerant, and air conditioner |
-
1990
- 1990-07-31 JP JP20314890A patent/JP2859718B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111023271A (en) * | 2019-12-31 | 2020-04-17 | 宁波奥克斯电气股份有限公司 | Adjustment device, system and control method of multi-line refrigerant, and air conditioner |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2859718B2 (en) | 1999-02-24 |
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