JPH109721A - Freezing cycle - Google Patents
Freezing cycleInfo
- Publication number
- JPH109721A JPH109721A JP15970196A JP15970196A JPH109721A JP H109721 A JPH109721 A JP H109721A JP 15970196 A JP15970196 A JP 15970196A JP 15970196 A JP15970196 A JP 15970196A JP H109721 A JPH109721 A JP H109721A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- refrigeration cycle
- removing device
- compressor
- low
- 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.)
- Withdrawn
Links
- 230000008014 freezing Effects 0.000 title abstract 3
- 238000007710 freezing Methods 0.000 title abstract 3
- 239000003507 refrigerant Substances 0.000 claims abstract description 80
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 35
- 238000005057 refrigeration Methods 0.000 claims description 34
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical group F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 abstract 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 11
- 238000001816 cooling Methods 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は弗化炭化水素系冷媒
を使用可能とした冷凍・空調製品の冷凍サイクルに関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigeration cycle of a refrigeration / air-conditioning product which can use a fluorocarbon-based refrigerant.
【0002】[0002]
【従来の技術】図6には、金属の腐食や潤滑油の劣化の
原因となる冷媒管路中の水分を除去するための水分除去
装置を備えた冷凍サイクルとして、特開平5−6607
5号で提案されているものの系統図が示されている。図
6において、1は圧縮機、2は凝縮器、3はレシーバ、
4は冷媒流量制御手段(膨張手段)、5は蒸発器であ
り、上記水分除去装置6は蒸発器5の下流側の低圧ガス
管路10に設置されている。2. Description of the Related Art FIG. 6 shows a refrigeration cycle equipped with a moisture removing device for removing moisture in a refrigerant pipe which causes corrosion of metal and deterioration of lubricating oil.
A system diagram of the one proposed in No. 5 is shown. In FIG. 6, 1 is a compressor, 2 is a condenser, 3 is a receiver,
4 is a refrigerant flow control means (expansion means), 5 is an evaporator, and the water removing device 6 is installed in the low-pressure gas line 10 on the downstream side of the evaporator 5.
【0003】上記冷凍サイクルにおいて、圧縮機1にて
高温・高圧に加圧されたガス冷媒は高圧ガス配管7を通
って凝縮器2に入り、ここで凝縮、液化しレシーバ3に
溜まる。次いでこの液冷媒は、高圧液配管8を通って冷
媒流量制御手段4に入り、ここで断熱膨張されて減圧さ
れ、低圧で乾き度の低い気液二相状態となった後、低圧
液配管9を通って蒸発器5に入り、ここで室内空気と熱
交換して蒸発し、低圧のガス冷媒となる。このガス冷媒
は低圧ガス管路10に設けられた水分除去装置6を通っ
て水分を除去され圧縮機1へと戻る。In the refrigerating cycle, the gas refrigerant pressurized to a high temperature and a high pressure by the compressor 1 enters the condenser 2 through the high pressure gas pipe 7, where it is condensed and liquefied and accumulated in the receiver 3. Next, the liquid refrigerant enters the refrigerant flow control means 4 through the high-pressure liquid pipe 8, where it is adiabatically expanded and decompressed to a low-pressure, low-dryness gas-liquid two-phase state. Into the evaporator 5 through which heat exchange with room air evaporates to become a low-pressure gas refrigerant. This gas refrigerant passes through the water removing device 6 provided in the low-pressure gas pipe 10 to remove moisture and returns to the compressor 1.
【0004】[0004]
【発明が解決しようとする課題】図5には、作動冷媒と
して弗化炭化水素系冷媒を使用した際における、図6に
示されるような蒸発器5下流の低圧ガス管路10に水分
除去装置6を設置した場合(図5のB線)と、これを設
置しない場合(図5のA線)との冷媒流量制御手段4を
流れる冷媒流量比率の時間変化が示されている。FIG. 5 shows a water removing device in a low pressure gas line 10 downstream of an evaporator 5 as shown in FIG. 6 when a fluorocarbon refrigerant is used as a working refrigerant. 6 shows the change over time of the ratio of the flow rate of the refrigerant flowing through the refrigerant flow control means 4 when the device 6 is installed (line B in FIG. 5) and when it is not installed (line A in FIG. 5).
【0005】図5に示されるように、上記冷媒使用の許
で水分除去装置6を、図6に示されるように、冷媒流量
制御手段4及び蒸発器5の下流の冷媒管路に設置した場
合(図5のB線)には、上記冷媒流量制御手段4の内壁
に異物の付着による閉塞が発生することにより、同制御
手段4を流れる冷媒流量が低下する。この流量減少によ
って圧縮機1の温度が上昇し、軸受部、運動部の焼付き
等の故障の発生をみることがある。[0005] As shown in FIG. 5, when the above-mentioned refrigerant is used, the water removing device 6 is installed in the refrigerant flow control means 4 and the refrigerant pipe downstream of the evaporator 5 as shown in FIG. At line B in FIG. 5, the flow rate of the refrigerant flowing through the refrigerant flow control unit 4 decreases due to the obstruction of the inner wall of the refrigerant flow control unit 4 due to the adhesion of foreign matter. Due to this decrease in the flow rate, the temperature of the compressor 1 rises, and failures such as seizure of the bearing portion and the moving portion may occur.
【0006】本発明の目的は、弗化炭化水素系冷媒の使
用時にあっても、冷媒循環管路の流量の減少を回避しつ
つ、冷媒管路中の水分の除去を可能とした冷凍サイクル
を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a refrigeration cycle capable of removing water from a refrigerant line while avoiding a decrease in the flow rate of the refrigerant circulation line even when a fluorocarbon refrigerant is used. To provide.
【0007】[0007]
【課題を解決するための手段】本発明は上記問題点を解
決するもので、その要旨とする手段は、圧縮機、凝縮
器、冷媒流量制御手段及び蒸発器を冷媒配管により接続
して冷凍サイクルを形成すると共に、作動冷媒として弗
化炭化水素系冷媒を用いてなる冷凍サイクルであって、
同サイクル中の低圧ガス管路に分岐回路を接続し、同回
路の端部に水分除去装置を設けてなることを特徴とする
冷凍サイクルにある。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and the gist of the invention is to connect a compressor, a condenser, a refrigerant flow rate control means, and an evaporator through a refrigerant pipe to a refrigeration cycle. And a refrigeration cycle using a fluorinated hydrocarbon-based refrigerant as a working refrigerant,
A refrigeration cycle is characterized in that a branch circuit is connected to a low-pressure gas line in the cycle, and a moisture removing device is provided at an end of the circuit.
【0008】また上記手段において、好ましくは、上記
水分除去装置を、上記圧縮機よりも高い位置に設置し、
あるいは、上記分岐回路に、上記圧縮機よりも高位置と
なる上げループを形成する。In the above means, preferably, the water removing device is installed at a position higher than the compressor.
Alternatively, a raising loop that is higher than the compressor is formed in the branch circuit.
【0009】上記手段によれば、冷凍サイクルの冷媒管
路中の水分は、水蒸気となって、低圧ガス管路から分岐
された分岐回路を通り水分除去装置に導入され、これの
捕捉部に吸着される。従って、上記手段によれば水分除
去装置が、冷媒が通過しない部位に設けられているの
で、従来のもののように、水分除去装置を設けたことに
よる冷媒流量制御手段の閉塞が回避され、冷媒流量の低
下の発生が防止される。これにより、冷媒流量の低下を
招くことなく冷媒中の水分を確実に除去することができ
る。According to the above means, the water in the refrigerant line of the refrigeration cycle is converted into water vapor, introduced into the water removing device through the branch circuit branched from the low-pressure gas line, and adsorbed on the trapping portion. Is done. Therefore, according to the above-described means, since the moisture removing device is provided in a portion through which the refrigerant does not pass, the blockage of the refrigerant flow control means due to the provision of the moisture removing device as in the conventional device is avoided, and the refrigerant flow rate is reduced. Is prevented from occurring. Thereby, it is possible to reliably remove the moisture in the refrigerant without causing a decrease in the refrigerant flow rate.
【0010】また、さらに具体的には、上記手段におい
て、上記水分除去装置を、上記分岐回路に対して、着脱
自在に設けてなる。かかる手段によれば、冷媒を冷凍サ
イクルの管路中に残留させた状態で水分除去装置の取外
し及び取付けが可能となり、整備性、取扱性が向上す
る。[0010] More specifically, in the above means, the water removing device is provided detachably with respect to the branch circuit. According to this means, the water removing device can be removed and attached in a state where the refrigerant remains in the pipeline of the refrigeration cycle, and the maintainability and handleability are improved.
【0011】また、本発明の要旨とする他の手段は、圧
縮機、四方弁、熱源側熱交換器、冷媒流量制御手段及び
利用側熱交換器を冷媒配管により接続してヒートポンプ
冷凍サイクルを形成すると共に、作動冷媒として弗化炭
化水素系冷媒を用いてなる冷凍サイクルであって、同サ
イクル中の低圧ガス管路に分岐回路を接続し、同回路の
端部に水分除去装置を設けてなる冷凍サイクルにある。
そして、好ましくは、上記手段において、上記低圧ガス
回路が、上記圧縮機と四方弁間の吸入ガス回路に構成さ
れる。Another aspect of the present invention is to form a heat pump refrigeration cycle by connecting a compressor, a four-way valve, a heat source side heat exchanger, a refrigerant flow control means, and a use side heat exchanger by refrigerant piping. And a refrigeration cycle using a fluorohydrocarbon-based refrigerant as a working refrigerant, wherein a branch circuit is connected to a low-pressure gas line in the cycle, and a moisture removing device is provided at an end of the circuit. In the refrigeration cycle.
Preferably, in the above means, the low-pressure gas circuit is configured as a suction gas circuit between the compressor and the four-way valve.
【0012】かかる手段によれば、水分除去装置に接続
される分岐回路は、四方弁の切り換えにより、冷房時、
暖房時の双方において低圧ガス管路から分岐されること
となり、冷・暖房双方の運転時において、冷媒流量の低
下を伴うことなく水分の除去が可能となる。According to this means, the branch circuit connected to the water removing device can switch the four-way valve during cooling,
The branch is made from the low-pressure gas pipeline both during heating and during the operation of both cooling and heating, water can be removed without a decrease in refrigerant flow rate.
【0013】[0013]
【発明の実施の形態】以下図1〜図4を参照して本発明
の実施形態につき詳細に説明する。図1には本発明の実
施の第1形態に係る冷凍サイクルの系統図が示されてい
る。図1において1はガス冷媒を圧縮する圧縮機、2は
同圧縮機1にて加圧され高圧ガス配管7を通ったガス冷
媒を冷却、液化する凝縮器、3はレシーバ、4は上記凝
縮器2から高圧液配管8を経た液冷媒を膨張、減圧せし
める冷媒流量制御手段(膨張手段)、5は上記制御手段
4から低圧液配管9を経た冷媒と室内空気とを熱交換し
て室内空気を冷却するとともに、冷媒を蒸発、気化せし
める蒸発器である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below in detail with reference to FIGS. FIG. 1 shows a system diagram of a refrigeration cycle according to a first embodiment of the present invention. In FIG. 1, 1 is a compressor for compressing a gas refrigerant, 2 is a condenser for cooling and liquefying the gas refrigerant pressurized by the compressor 1 and passing through a high-pressure gas pipe 7, 3 is a receiver, 4 is the condenser described above. Refrigerant flow rate control means (expansion means) 5 for expanding and decompressing the liquid refrigerant from 2 through the high-pressure liquid pipe 8, and heat exchange between the refrigerant through the low-pressure liquid pipe 9 and the indoor air from the control means 4 to convert the indoor air. An evaporator that cools and evaporates and vaporizes the refrigerant.
【0014】10は上記蒸発器5の冷媒出口と圧縮機1
の吸込口とを接続する低圧ガス配管、11は同ガス配管
10の途中から分岐された分岐回路である。そして同分
岐回路11の管端部には上記低圧ガス配管10を流れる
冷媒中の水分を分離する水分除去装置6が取付けられて
いる。同水分除去装置6は、上記分岐回路11の圧縮機
1よりも充分に高い位置(高水頭の位置)に取付けられ
る。Reference numeral 10 denotes a refrigerant outlet of the evaporator 5 and the compressor 1
A low-pressure gas pipe 11 connecting the suction port of the gas pipe 10 and a branch circuit branched from the middle of the gas pipe 10. At the pipe end of the branch circuit 11, a moisture removing device 6 for separating moisture in the refrigerant flowing through the low-pressure gas pipe 10 is attached. The water removing device 6 is mounted at a position (high water head position) sufficiently higher than the compressor 1 in the branch circuit 11.
【0015】上記のように構成された冷凍サイクルにお
いて、圧縮機1にて高温・高圧に加圧されたガス冷媒
は、高圧ガス配管7を通って凝縮器2に入り、ここで凝
縮液化しレシーバ3に溜まる。次いで、この液冷媒は、
高圧液配管8を通って冷媒流量制御手段4に入り、ここ
で断熱膨張されて減圧され、低圧で乾き度の低い気液二
相状態となった後、低圧液配管9を通って蒸発器5に入
り、ここで室内空気と熱交換して蒸発し、低圧のガス冷
媒となる。このガス冷媒は低圧ガス配管10を通って水
分除去装置6に連なる分岐回路11の分岐部21を通っ
て圧縮機1に戻される。In the refrigeration cycle configured as described above, the gas refrigerant pressurized to a high temperature and a high pressure by the compressor 1 enters the condenser 2 through the high pressure gas pipe 7, where it is condensed and liquefied. Collect in 3. This liquid refrigerant then
The refrigerant enters the refrigerant flow control means 4 through the high-pressure liquid pipe 8, where it is adiabatically expanded and decompressed to a low-pressure, low-dryness gas-liquid two-phase state. , Where it exchanges heat with room air and evaporates to become a low-pressure gas refrigerant. This gas refrigerant is returned to the compressor 1 through the branch part 21 of the branch circuit 11 connected to the moisture removing device 6 through the low-pressure gas pipe 10.
【0016】この際において、低圧ガス配管10内の水
分は水蒸気となって分岐回路11内を上昇し、水分除去
装置6の捕捉部に吸着される。従って、上記実施形態に
よれば、水分除去装置6が冷凍サイクルの運転中に冷媒
が通過しない部位に設けられているので、従来のものの
ように水分除去装置6を設けたことによる冷媒流路の低
下は発生しない。また、冷凍サイクルの運転中におい
て、低圧ガス配管10を流れる冷媒が分岐回路11を通
って水分除去装置6に流入して充満することはない。At this time, the water in the low-pressure gas pipe 10 becomes steam and rises in the branch circuit 11, and is adsorbed by the trapping section of the water removing device 6. Therefore, according to the above-described embodiment, since the water removing device 6 is provided in a portion through which the refrigerant does not pass during the operation of the refrigeration cycle, the refrigerant flow path due to the provision of the water removing device 6 as in the conventional device is reduced. No degradation occurs. Further, during the operation of the refrigeration cycle, the refrigerant flowing through the low-pressure gas pipe 10 does not flow into the moisture removing device 6 through the branch circuit 11 and is not filled.
【0017】図2には本発明の実施の第2形態に係る冷
凍サイクルの系統図が示されている。この実施形態にお
いては、上記分岐回路11の管端に取付けられる水分除
去装置6の高さ位置を上記圧縮機1よりも低い位置とす
るとともに、上記分岐回路11を、これに圧縮機1より
も水頭的に高位置となる上げループのループ部11aを
形成してから上記水分除去装置6に接続している。その
他の構成は図1に示される第1形態と同様である。FIG. 2 is a system diagram of a refrigeration cycle according to a second embodiment of the present invention. In this embodiment, the height position of the moisture removing device 6 attached to the pipe end of the branch circuit 11 is set to a position lower than that of the compressor 1, and the branch circuit 11 is After forming a loop portion 11a of a raising loop which is at a high position in terms of the water head, it is connected to the water removing device 6. Other configurations are the same as those of the first embodiment shown in FIG.
【0018】図3には本発明の実施の第3形態に係る冷
凍サイクルが示されている。この実施形態においては、
上記分岐回路11の上記水分除去装置6に近い部位に開
閉弁12を介装するとともに、同開閉弁12と水分除去
装置6との間にフレア接続による接続部13を設けてい
る。従ってこの実施形態においては、開閉弁12を閉じ
て水分除去装置6と低圧ガス配管10側との接続を遮断
し、フレア接続部13にて水分除去装置6を取り外しあ
るいは取付けることにより、冷媒を冷媒管路に残留させ
たまま、水分除去装置6の着脱がきわめて容易にでき
る。FIG. 3 shows a refrigeration cycle according to a third embodiment of the present invention. In this embodiment,
An on-off valve 12 is interposed in a portion of the branch circuit 11 close to the moisture removing device 6, and a connecting portion 13 by flare connection is provided between the on-off valve 12 and the moisture removing device 6. Therefore, in this embodiment, the on-off valve 12 is closed to cut off the connection between the moisture removal device 6 and the low-pressure gas pipe 10 side, and the moisture removal device 6 is detached or attached at the flare connection portion 13 so that the coolant is cooled. The attachment and detachment of the water removing device 6 can be extremely easily performed while remaining in the pipeline.
【0019】図4には本発明の実施の第4形態に係る冷
凍サイクルが示されている。この実施形態においては、
圧縮機1の出入口の高圧ガス配管7及び低圧ガス配管1
0の間に冷房・暖房切換用の四方弁14を設けるととも
に、上記四方弁14と圧縮機1との間の低圧ガス配管1
0から分岐された分岐回路11を設け、同分岐回路11
の端部に水分除去装置6を取付けている。FIG. 4 shows a refrigeration cycle according to a fourth embodiment of the present invention. In this embodiment,
High pressure gas pipe 7 and low pressure gas pipe 1 at the entrance and exit of compressor 1
0, a four-way valve 14 for switching between cooling and heating is provided, and a low-pressure gas pipe 1 between the four-way valve 14 and the compressor 1 is provided.
A branch circuit 11 branched from 0 is provided.
The water removing device 6 is attached to the end of the.
【0020】この実施形態においては、冷房時には実線
矢印のように冷媒が流れ、四方弁14を暖房側に切り換
えた際には圧縮機1から四方弁14を経て破線矢印のよ
うに冷媒が流れるが、冷房時、暖房時ともに低圧となる
四方弁14と圧縮機1との間から分岐回路11を分岐し
て水分除去装置6に接続しているので、上記第1〜第3
形態と同様な水分除去作用が得られる。In this embodiment, during cooling, the refrigerant flows as indicated by the solid arrow, and when the four-way valve 14 is switched to the heating side, the refrigerant flows from the compressor 1 through the four-way valve 14 as indicated by the dashed arrow. Since the branch circuit 11 is branched from between the four-way valve 14 and the compressor 1 which have a low pressure during both cooling and heating, and is connected to the water removing device 6,
The same water removing action as in the embodiment can be obtained.
【0021】また、圧縮機1が低圧ハウジングであれ
ば、圧縮機1のドーム内は低圧であるので、上記分岐回
路11を圧縮機1のドームから分岐させてもよい。If the compressor 1 is a low-pressure housing, the inside of the dome of the compressor 1 is at a low pressure, so that the branch circuit 11 may be branched from the dome of the compressor 1.
【0022】尚、上記水分除去装置6の周囲と低圧ガス
配管10との間は水分除去装置6による低圧ガス配管1
0からの水蒸気の吸着によって水蒸気分圧差が生ずるの
で、上記各実施形態ともに、水分除去装置6の設置高さ
に拘わらず、冷凍サイクル内の水分の除去は可能であ
る。A low-pressure gas pipe 1 by the moisture removing device 6 is provided between the periphery of the moisture removing device 6 and the low-pressure gas piping 10.
Since the difference in partial pressure of water vapor is caused by the adsorption of water vapor from zero, the water in the refrigeration cycle can be removed regardless of the installation height of the water removal device 6 in each of the above embodiments.
【0023】[0023]
【発明の効果】本発明は以上のように構成されており、
本発明によれば、冷凍サイクル運転中において、水分除
去装置6を冷媒が通過することがなく、冷媒流量制御手
段への異物の付着が防止され、冷媒流量の低下を回避し
つつ水分の除去を行うことができる。The present invention is configured as described above.
According to the present invention, during the operation of the refrigeration cycle, the refrigerant does not pass through the water removing device 6 and foreign matter is prevented from adhering to the refrigerant flow rate control means. It can be carried out.
【0024】また冷凍サイクル運転中に、水分除去装置
が冷媒で満たされることがないので、この面からも上記
異物の付着防止効果が得られる。In addition, during the operation of the refrigeration cycle, the water removing device is not filled with the refrigerant, so that the effect of preventing the adhesion of the foreign matter can be obtained from this aspect as well.
【0025】また請求項4のように構成すれば、冷媒を
冷凍サイクルの管路中に残留させたまま水分除去装置の
取外し、取付けが可能となり、整備性、取扱性の向上が
得られる。According to the fourth aspect of the present invention, it is possible to remove and attach the water removing device while the refrigerant remains in the pipeline of the refrigeration cycle, so that maintenance and handling can be improved.
【0026】さらに請求項5〜6のように構成すれば、
冷・暖房双方の運転時において冷媒流量の低下をみるこ
となく水分の除去を確実に行うことができる。Further, according to the fifth and sixth aspects,
Moisture can be reliably removed without any decrease in the flow rate of the refrigerant during both cooling and heating operations.
【図1】本発明の実施の第1形態に係る冷凍サイクルの
系統図。FIG. 1 is a system diagram of a refrigeration cycle according to a first embodiment of the present invention.
【図2】本発明の実施の第2形態を示す図1応当図。FIG. 2 is an equivalent view of FIG. 1 showing a second embodiment of the present invention.
【図3】本発明の実施の第3形態を示す図1応当図。FIG. 3 is an equivalent view of FIG. 1 showing a third embodiment of the present invention.
【図4】本発明の実施の第4形態を示す図1応当図。FIG. 4 is an equivalent view of FIG. 1 showing a fourth embodiment of the present invention.
【図5】冷媒流量制御手段の流量線図。FIG. 5 is a flow chart of refrigerant flow control means.
【図6】従来の冷凍サイクルを示す図1応当図。FIG. 6 is an equivalent view of FIG. 1 showing a conventional refrigeration cycle.
1 圧縮機 2 凝縮器 3 レシーバ 4 冷媒流量制御手段 5 蒸発器 6 水分除去装置 7 高圧ガス配管 8 高圧液配管 9 低圧液配管 10 低圧ガス配管 11 分岐回路 12 開閉弁 14 四方弁 DESCRIPTION OF SYMBOLS 1 Compressor 2 Condenser 3 Receiver 4 Refrigerant flow control means 5 Evaporator 6 Water removal device 7 High-pressure gas pipe 8 High-pressure liquid pipe 9 Low-pressure liquid pipe 10 Low-pressure gas pipe 11 Branch circuit 12 On-off valve 14 Four-way valve
Claims (6)
蒸発器を冷媒配管により接続して冷凍サイクルを形成す
ると共に、作動冷媒として弗化炭化水素系冷媒を用いて
なる冷凍サイクルであって、同サイクル中の低圧ガス管
路に分岐回路を接続し、同回路の端部に水分除去装置を
設けてなることを特徴とする冷凍サイクル。1. A refrigeration cycle comprising a compressor, a condenser, a refrigerant flow control means, and an evaporator connected by refrigerant piping to form a refrigeration cycle, and using a fluorocarbon refrigerant as a working refrigerant. A refrigeration cycle comprising a branch circuit connected to a low-pressure gas line in the cycle, and a moisture removing device provided at an end of the circuit.
高い位置に設置してなる請求項1に記載の冷凍サイク
ル。2. The refrigeration cycle according to claim 1, wherein the water removing device is installed at a position higher than the compressor.
置となる上げループを形成してなる請求項1に記載の冷
凍サイクル。3. The refrigeration cycle according to claim 1, wherein a raising loop that is higher than the compressor is formed in the branch circuit.
して着脱自在に設けてなる請求項1に記載の冷凍サイク
ル。4. The refrigeration cycle according to claim 1, wherein the water removing device is provided detachably from the branch circuit.
流量制御手段及び利用側熱交換器を冷媒配管により接続
してヒートポンプ冷凍サイクルを形成すると共に、作動
冷媒として弗化炭化水素系冷媒を用いてなる冷凍サイク
ルであって、同サイクル中の低圧ガス管路に分岐回路を
接続し、同回路の端部に水分除去装置を設けてなる冷凍
サイクル。5. A heat pump refrigeration cycle is formed by connecting a compressor, a four-way valve, a heat source side heat exchanger, a refrigerant flow control means, and a use side heat exchanger by a refrigerant pipe, and a fluorinated hydrocarbon system as an operating refrigerant. A refrigeration cycle using a refrigerant, wherein a branch circuit is connected to a low-pressure gas pipe in the cycle, and a moisture removing device is provided at an end of the circuit.
弁間の吸入ガス回路である請求項5に記載の冷凍サイク
ル。6. The refrigeration cycle according to claim 5, wherein the low-pressure gas circuit is a suction gas circuit between the compressor and a four-way valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15970196A JPH109721A (en) | 1996-06-20 | 1996-06-20 | Freezing cycle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15970196A JPH109721A (en) | 1996-06-20 | 1996-06-20 | Freezing cycle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH109721A true JPH109721A (en) | 1998-01-16 |
Family
ID=15699431
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15970196A Withdrawn JPH109721A (en) | 1996-06-20 | 1996-06-20 | Freezing cycle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH109721A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4845093A (en) * | 1984-07-24 | 1989-07-04 | Ishihara Sangyo Kaisha Ltd. | N-benzoyl-N'-pyridazinyloxyphenyl urea compounds, and antitumorous compositions containing them, and process for their preparation |
| JP2023037822A (en) * | 2021-09-06 | 2023-03-16 | パナソニックIpマネジメント株式会社 | air conditioner |
-
1996
- 1996-06-20 JP JP15970196A patent/JPH109721A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4845093A (en) * | 1984-07-24 | 1989-07-04 | Ishihara Sangyo Kaisha Ltd. | N-benzoyl-N'-pyridazinyloxyphenyl urea compounds, and antitumorous compositions containing them, and process for their preparation |
| JP2023037822A (en) * | 2021-09-06 | 2023-03-16 | パナソニックIpマネジメント株式会社 | air conditioner |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20030902 |