JPH0455667A - Moisture removing device for refrigerating device - Google Patents

Moisture removing device for refrigerating device

Info

Publication number
JPH0455667A
JPH0455667A JP16753790A JP16753790A JPH0455667A JP H0455667 A JPH0455667 A JP H0455667A JP 16753790 A JP16753790 A JP 16753790A JP 16753790 A JP16753790 A JP 16753790A JP H0455667 A JPH0455667 A JP H0455667A
Authority
JP
Japan
Prior art keywords
moisture
liquid
refrigerant
concentration
water
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
Application number
JP16753790A
Other languages
Japanese (ja)
Inventor
Hisasuke Sakakibara
久介 榊原
Shin Honda
伸 本田
Keiichi Kitamura
圭一 北村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Denso Corp
Original Assignee
NipponDenso Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by NipponDenso Co Ltd filed Critical NipponDenso Co Ltd
Priority to JP16753790A priority Critical patent/JPH0455667A/en
Publication of JPH0455667A publication Critical patent/JPH0455667A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To remove moisture surely utilizing the characteristics of refrigerant by a method wherein liquid refrigerant is molten into high moisture concentration liquid, flowing out of a refrigerant evaporator, to reduce the concentration of saturated moisture of the liquid while free water, generated by the reduction, is retained by a moisture retaining member. CONSTITUTION:High moisture concentration liquid, flowing out of a refrigerant evaporator 6, flows into a reserving chamber 8 as it is and liquid refrigerant is guided through a refrigerant introducing pipe 9b. According to this operation, the mixed molar ratio of the high moisture concentration liquid is moved to the side of refrigerant and the concentration of saturated moisture in the liquid is reduced whereby liberated water is generated from the liquid. The liberated water and the liquid pass through the holes 10b of a pushing plate 10c and only the liberated water is retained by a moisture retaining member 10a while the liquid, from which the liberated water is removed, is returned into a main flow through a discharging pipe 10d. The liberated water, retained by the moisture retaining member 10a, is discharged to the outside of a refrigerating device 1 after passing through a selective penetration film 12 and the moisture, removed from the inside of a cycle, can be discharged to the outside of the refrigerating device 1 whereby the inside of the cycle can be kept in a low moisture concentration against the invasion of moisture at all times.

Description

【発明の詳細な説明】 し産業上の利用分野1 本発明は、冷凍装置内に浸入した水分を除去するための
冷凍装置用水分除去装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application 1 The present invention relates to a moisture removal device for a refrigeration system for removing moisture that has entered the refrigeration system.

[従来の技術] 一般に、カーエアコン用の冷凍サイクルでは、冷媒配管
の一部にゴムホースを使用するなめ、このゴムホースを
通して、冷凍サイクル内に水分が浸入する。
[Prior Art] Generally, in a refrigeration cycle for a car air conditioner, a rubber hose is used as a part of the refrigerant piping, and moisture infiltrates into the refrigeration cycle through this rubber hose.

サイクル内の水分濃度が高くなると、冷凍サイクルを構
成する金属部分で内部腐食を引き起こしたり、膨張弁で
の氷結によって冷却性能の低下を招く等の不具合を生じ
る。
When the moisture concentration in the cycle increases, problems such as internal corrosion in the metal parts that make up the refrigeration cycle and a decrease in cooling performance due to freezing at the expansion valve occur.

そこで、従来では、例えば、冷凍サイクルのレシーバ内
に乾燥剤を封入してサイクル内の除湿を行っている。
Therefore, conventionally, for example, a desiccant is sealed in the receiver of a refrigeration cycle to dehumidify the cycle.

また、冷凍サイクルの蒸発器下流の低圧配管に乾燥剤を
装着し、冷媒ガス中に混入した水分を除去しようとする
ものも提案されている。
Furthermore, a method has been proposed in which a desiccant is installed in the low-pressure pipe downstream of the evaporator of the refrigeration cycle to remove moisture mixed in the refrigerant gas.

[発明が解決しようとする課題] 上記のような乾燥剤を使用する方法では、吸湿能力に限
界があり、水分を吸収するにしたがって取り残す水分量
が増大する。従って、浸入してくる水分に対してサイク
ル内を低水分濃度に保つためには、多量の乾燥剤を封入
しておく必要がある。
[Problems to be Solved by the Invention] In the method using a desiccant as described above, there is a limit to the moisture absorption ability, and as moisture is absorbed, the amount of moisture left behind increases. Therefore, in order to keep the moisture concentration in the cycle at a low level against invading moisture, it is necessary to enclose a large amount of desiccant.

ところが、乾燥剤を多量に使用することによりレシーバ
が大型化して車両I・\の搭載性が低下するため、実際
には、適宜、乾燥剤の交換を必要とする。
However, using a large amount of desiccant increases the size of the receiver and reduces the ease of mounting it on the vehicle I/\, so in reality, the desiccant needs to be replaced as appropriate.

また、低圧配管に乾燥剤を装着したものでは、従来広く
用いられる冷媒(R42)が気相において高い飽和水分
濃度を示すため、この気相の冷媒から水分を除去するた
めに大量で強力な乾燥剤を要するという問題点があった
In addition, in low-pressure piping equipped with a desiccant, since the conventionally widely used refrigerant (R42) exhibits a high saturated moisture concentration in the gas phase, a large amount of powerful drying is required to remove moisture from this gas phase refrigerant. There was a problem in that it required a chemical agent.

また、従来一般にカーエアコンには上記のR12が冷媒
として用いられていたが、近年R134aのように、気
相の飽和水分濃度より液相の飽和水分濃度の方が高い(
R,12とは逆の特性)新冷媒がカーエアコン用に注目
されている。ところがR134aの水分特性では従来の
ようなレシーバ内の乾燥剤では十分な除湿効果が得られ
ないという問題点があった。そこで本発明は、上記のご
とき従来技術の問題点に鑑み、気相の飽和水分濃度より
液相の飽和水分濃度の方が高いという一部冷媒の特性を
利用して確実な水分除去を行うことのできる冷凍装置用
水分除去装置を提供することにある。
In addition, in the past, the above-mentioned R12 was generally used as a refrigerant in car air conditioners, but in recent years, R134a, which has a higher saturated water concentration in the liquid phase than in the gas phase (
A new refrigerant (with characteristics opposite to those of R, 12) is attracting attention for use in car air conditioners. However, due to the moisture characteristics of R134a, there was a problem in that a sufficient dehumidification effect could not be obtained using a conventional desiccant in the receiver. Therefore, in view of the problems of the prior art as described above, the present invention aims to perform reliable moisture removal by utilizing the characteristic of some refrigerants that the saturated moisture concentration in the liquid phase is higher than the saturated moisture concentration in the gas phase. An object of the present invention is to provide a moisture removal device for a refrigeration equipment that can perform the following functions.

[課題を解決するための手段] 本発明は上記目的を達成するために、気相の飽和水分濃
度より液相の飽和水分濃度の方が高い水分特性を有する
冷媒と親水性の高い冷凍機油とを使用する冷凍装置に適
用され、この冷凍装置の冷媒蒸発器より流出した高水分
濃度液を貯留する貯留室と、この貯留室内に液冷媒を導
き、この液冷媒を前記貯留室内の高水分濃度液に溶解さ
せることにより、前記高水分濃度液より遊離水を発生さ
せる遊離水発生手段と、水分保持材を備え、発生した遊
離水を前記水分保持材に保持させる水分保持手段とから
成ることを技術的手段とする。
[Means for Solving the Problems] In order to achieve the above object, the present invention uses a refrigerant having moisture characteristics in which the saturated moisture concentration in the liquid phase is higher than the saturated moisture concentration in the gas phase, and a highly hydrophilic refrigerating machine oil. It is applied to a refrigeration system using a refrigeration system, and includes a storage chamber for storing a high moisture concentration liquid flowing out from a refrigerant evaporator of this refrigeration system, and a liquid refrigerant is guided into this storage chamber, and the liquid refrigerant is used to reduce the high moisture concentration in the storage chamber. The method comprises a free water generating means that generates free water from the high water concentration liquid by dissolving it in a liquid, and a water retaining means that includes a moisture retaining material and causes the generated free water to be retained in the moisture retaining material. Use technical means.

[作用] 上記構成よりなる本発明は、冷凍装置に使用される冷媒
の水分特性が、気相の飽和水分濃度より液相の水分濃度
の方が高いため、冷媒蒸発器で冷媒が蒸発するにしたが
い、液中(冷凍機油と液冷媒との混合液)の水分濃度が
高くなる。
[Function] The present invention having the above-mentioned configuration has a moisture characteristic of the refrigerant used in the refrigeration system, and the moisture concentration in the liquid phase is higher than the saturated moisture concentration in the gas phase. Therefore, the water concentration in the liquid (mixture of refrigerating machine oil and liquid refrigerant) increases.

そこで、冷媒蒸発器より流出する高水分濃度液を貯留室
で貯留し、その高水分濃度液に液冷媒を溶解させ、液の
飽和水分濃度を下げることによって遊離水を発生させる
ことができる。
Therefore, free water can be generated by storing the high water concentration liquid flowing out from the refrigerant evaporator in a storage chamber, dissolving the liquid refrigerant in the high water concentration liquid, and lowering the saturated water concentration of the liquid.

この発生した遊離水を、水分保持材で保持することによ
り、冷凍装置内の水分を除去する。
By retaining this generated free water with a moisture retaining material, moisture within the refrigeration system is removed.

[発明の効果] 上記作用を有する本発明によれば、冷媒の水分特性と冷
凍機油の水分特性とを利用して遊離水を発生させ、その
発生した遊離水を水分保持材で保持し、冷凍装置内に浸
入した水分を除去するため、従来のように多量の乾燥剤
を使用することなく、確実な水分除去を行うことができ
る。
[Effects of the Invention] According to the present invention having the above-mentioned effects, free water is generated using the moisture characteristics of the refrigerant and the moisture characteristics of the refrigerating machine oil, and the generated free water is retained by the moisture retaining material. Since moisture that has entered the device is removed, moisture can be reliably removed without using a large amount of desiccant as in the conventional method.

[実施例] 次に、本発明の冷凍装置用水分除去装置を図面に示す一
実施例に基づき説明する。
[Example] Next, a moisture removal device for a refrigeration equipment according to the present invention will be described based on an example shown in the drawings.

第1図は水分除去装置を適用した冷凍装置の冷凍サイク
ル図である。
FIG. 1 is a refrigeration cycle diagram of a refrigeration system to which a moisture removal device is applied.

本実施例の冷凍装置11は、冷媒圧縮機2、冷媒凝縮器
3、レシーバ4、膨張弁5、および冷媒蒸発器6の各機
能部品より構成され、冷媒配管7で環状に接続された周
知の構造を有する。
The refrigeration system 11 of this embodiment is composed of functional parts such as a refrigerant compressor 2, a refrigerant condenser 3, a receiver 4, an expansion valve 5, and a refrigerant evaporator 6, which are connected in an annular manner by a refrigerant pipe 7. Has a structure.

通常、カーエアコンなどの冷凍サイクルでは、フロン系
の冷媒R12が使用されるが、この冷凍装置1には、気
相の飽和水分濃度より液相の飽和水分濃度の方が高い水
分特性を有する冷媒、例えばR134a、またはR22
が使用される。また、冷凍機油(冷媒圧縮機2の潤滑油
)には、親水性の高いもの、例えばP A、 G系のも
のが使用される。
Normally, a fluorocarbon-based refrigerant R12 is used in a refrigeration cycle such as a car air conditioner. , for example R134a, or R22
is used. Further, as the refrigerating machine oil (lubricating oil for the refrigerant compressor 2), a highly hydrophilic oil, such as a PA or G type oil, is used.

従って、本実施例の冷凍装置1では、第3図の温度−組
成図に示すように、冷媒蒸発器6で冷媒が蒸発するに従
い、液中(冷凍機油と液冷媒との混合液中)の水分濃度
が高くなるため、冷媒蒸発器6からは、冷凍機油に液冷
媒が溶解した状態の高水分濃度液が流出することになる
Therefore, in the refrigeration system 1 of this embodiment, as the refrigerant evaporates in the refrigerant evaporator 6, as shown in the temperature-composition diagram of FIG. Since the moisture concentration increases, a high moisture concentration liquid in which liquid refrigerant is dissolved in refrigerating machine oil flows out from the refrigerant evaporator 6.

この冷凍装置1に適用される水分除去装置は、冷媒蒸発
器6より流出しな高水分濃度液を貯留する貯留室(第2
図参照)8と、この貯留室8内に液冷媒を導き、この液
冷媒を貯留室8内の高水分濃度液に溶解させることによ
って、高水分濃度液より遊離水を発生させる遊離水発生
手段9と、水分保持材10aを備え、発生した遊離水を
水分保持材10aに保持させる水分保持手段(第2図参
照)10とから構成されている。
The moisture removal device applied to this refrigeration device 1 has a storage chamber (a second
(see figure) 8, and a free water generating means for introducing a liquid refrigerant into the storage chamber 8 and dissolving the liquid refrigerant in the high water concentration liquid in the storage chamber 8 to generate free water from the high water concentration liquid. 9, and a moisture retaining means (see FIG. 2) 10, which is provided with a moisture retaining material 10a and causes the generated free water to be retained in the moisture retaining material 10a.

貯留室8は、冷媒蒸発器6の下流で、第2図に示すよう
に、冷媒配管7の下側に接続して設けられ、冷媒蒸発器
6を流出した高水分濃度液が、そのまま貯留室8内に流
入するように構成されている。なお、第2図は水分除去
装置の要部断面図である。
The storage chamber 8 is provided downstream of the refrigerant evaporator 6 and connected to the lower side of the refrigerant pipe 7, as shown in FIG. 8. In addition, FIG. 2 is a sectional view of the main part of the moisture removal device.

遊離水発生手段9は、冷媒蒸発器6の上流で液冷媒を溜
める液溜め室9aと、この液溜め室9aと貯留室8とを
連絡する冷媒導入管9bと、この冷媒導入管9bの途中
に設けられた流量調整弁9Cとから構成される。流量調
整弁9Cは、貯留室8の過熱度によって、その弁開度が
制御されるもので、貯留室8内の温度変化を圧力変化と
して伝える感熱筒9dとキャピラリチューブ9Cを備え
る。
The free water generating means 9 includes a liquid storage chamber 9a that stores liquid refrigerant upstream of the refrigerant evaporator 6, a refrigerant introduction pipe 9b that connects the liquid storage chamber 9a and the storage chamber 8, and a refrigerant introduction pipe 9b that connects the liquid refrigerant to the storage chamber 8. It is composed of a flow rate adjustment valve 9C provided in the. The flow rate regulating valve 9C has its valve opening degree controlled depending on the degree of superheating of the storage chamber 8, and includes a heat-sensitive cylinder 9d and a capillary tube 9C that transmit temperature changes in the storage chamber 8 as pressure changes.

この遊離水発生手段9は、冷凍機油と液冷媒との混合モ
ル比に対する液中の飽和水分濃度を見ると、第4図に示
すように、混合モル比が冷媒側へ移動するにつれて飽和
水分濃度が低下することから、貯留室8内に液冷媒を導
いて高水分濃度液の混合モル比を冷媒側へ移動させ、飽
和水分濃度を下げることで遊離水を発生させるものであ
る。
When looking at the saturated water concentration in the liquid with respect to the mixed molar ratio of refrigerating machine oil and liquid refrigerant, the free water generating means 9 can be used to increase the saturated water concentration as the mixed molar ratio moves toward the refrigerant side, as shown in FIG. Since the liquid refrigerant is introduced into the storage chamber 8, the mixing molar ratio of the high water concentration liquid is shifted to the refrigerant side, and the saturated water concentration is lowered, thereby generating free water.

水分保持手段10は、貯留室8の底部に配設された水分
保持材10a  (例えば、グラスウール)と、この水
分保持材10aを固定するとともに、多数の孔10bが
設けられた押え板10Cと、遊離水の取り除かれた液を
主流中へ戻すための排出管10dから構成される。
The moisture retaining means 10 includes a moisture retaining material 10a (for example, glass wool) disposed at the bottom of the storage chamber 8, a holding plate 10C that fixes the moisture retaining material 10a and is provided with a large number of holes 10b. It consists of a discharge pipe 10d for returning the liquid from which free water has been removed into the mainstream.

この水分保持手段10は、排出管10dの上流側と下流
側との差圧を利用して水分保持材10aに遊離水を保持
させるもので、多数の孔10bを通過した遊離水と液(
冷凍機油+液冷媒)は、遊離水のみが水分保持材10a
で保持され、残りの液は、排出管101jを通って主流
中に戻され、冷媒配管7を流れるガス冷媒ととともに、
冷媒圧縮機2に吸引される。
This moisture retaining means 10 uses the differential pressure between the upstream side and the downstream side of the discharge pipe 10d to retain free water in the moisture retaining material 10a, and the free water and liquid (
Refrigerating machine oil + liquid refrigerant), only free water is the moisture retaining material 10a
The remaining liquid is returned to the main stream through the discharge pipe 101j, and together with the gas refrigerant flowing through the refrigerant pipe 7,
The refrigerant is sucked into the refrigerant compressor 2.

本実施例では、水分保持材10aで保持した遊離水を冷
凍袋■1外へ放出するために、水分保持材tOaの底面
側に外部と連通ずる開口部11を形成し、その開口部1
1に、水を透しやすく冷媒を透しにくい選択透過膜(例
えば、ポリイミド膜)12が配設されている。
In this embodiment, in order to release the free water retained by the moisture retaining material 10a to the outside of the freezer bag 1, an opening 11 communicating with the outside is formed on the bottom side of the moisture retaining material tOa.
1 is provided with a selectively permeable membrane (for example, a polyimide membrane) 12 that easily allows water to pass through but does not allow refrigerant to pass through.

次に、本実施例の作動を説明する。Next, the operation of this embodiment will be explained.

膨脂弁5で減圧された冷媒が冷媒蒸発器6で蒸発する際
に、冷媒蒸発器6の中では、第3図の温度−組成図にお
いて、矢印で示すように、冷媒の蒸発に従い、液中の水
分濃度が高くなる。
When the refrigerant whose pressure has been reduced by the expansion valve 5 is evaporated in the refrigerant evaporator 6, in the refrigerant evaporator 6, as shown by the arrow in the temperature-composition diagram of FIG. The water concentration inside increases.

このとき、本実施例の冷凍装置1では、親水性の高い冷
凍機油を使用していることから、冷媒蒸発器6からは、
高水分濃度の液(冷凍機油に液冷媒が溶解した状W)が
流出することになる。
At this time, since the refrigeration system 1 of this embodiment uses highly hydrophilic refrigeration oil, the refrigerant evaporator 6
A liquid with high moisture concentration (liquid refrigerant dissolved in refrigerating machine oil) will flow out.

この冷媒蒸発器6から流出した高水分濃度液は、そのま
ま貯留室8内に流入し、冷媒導入管9bを介して導かれ
た液冷媒と混合する。これにより、高水分濃度液の混合
モル比が冷媒側へ移動し、液中の飽和水分濃度が低下す
るため、液中よつ遊離水が発生する。
The high moisture concentration liquid flowing out from the refrigerant evaporator 6 flows into the storage chamber 8 as it is, and mixes with the liquid refrigerant introduced through the refrigerant introduction pipe 9b. As a result, the mixing molar ratio of the high water concentration liquid shifts to the refrigerant side, and the saturated water concentration in the liquid decreases, so that free water is generated in the liquid.

この遊離水と液とは、押え板10cの孔10bを通り、
水分保持材10aで遊離水のみ保持され、遊離水の取り
除かれた液が、排出管10dを介して主流中に戻される
This free water and liquid pass through the hole 10b of the holding plate 10c,
Only free water is retained by the moisture retaining material 10a, and the liquid from which the free water has been removed is returned to the mainstream via the discharge pipe 10d.

水分保持材10aで保持された遊離水は、選択透過膜1
2を通過して冷凍装置1の外部へ放出され、主流中に戻
された液は、冷媒蒸発器6より流出したガス冷媒ととも
に、冷媒圧縮機2に吸引される。
The free water retained by the moisture retaining material 10a is transferred to the selectively permeable membrane 1.
The liquid that passes through the refrigerant evaporator 2 and is discharged to the outside of the refrigeration device 1 and returned to the mainstream is sucked into the refrigerant compressor 2 together with the gas refrigerant that has flowed out from the refrigerant evaporator 6.

このように、本実施例では、サイクル内がら除去した水
分を冷凍装置1の外部へ放出することができるため、水
分の浸入に対しても、常にサイクル内を低水分濃度に保
つことができる。
In this manner, in this embodiment, the water removed from the inside of the cycle can be released to the outside of the refrigeration apparatus 1, so that the inside of the cycle can always be kept at a low water concentration even when water enters.

また、本実施例の水分除去装置は、多量の乾燥剤を使用
する必要がなく、コンパクトで、従来のように交換や点
検などの定期的なメンテナンスを必要としない。
Further, the moisture removal device of this embodiment does not require the use of a large amount of desiccant, is compact, and does not require periodic maintenance such as replacement or inspection unlike conventional devices.

次に、本発明の第2実施例を説明する。Next, a second embodiment of the present invention will be described.

第5図は水分除去装置を適用した冷凍装置1の冷凍サイ
クル図、第6図は水分除去装置の要部断面図である。
FIG. 5 is a refrigeration cycle diagram of the refrigeration system 1 to which the moisture removal device is applied, and FIG. 6 is a sectional view of the main parts of the moisture removal device.

上記の第1実施例では、貯留室8の高水分濃度液に、直
接液冷媒を混合させることで遊離水を発生させたが、本
実施例では、貯留室8の高水分濃度液を冷却して、主流
中を流れるガス冷媒を液化して溶は込ませることにより
、液中の飽和水分濃度を下げて、遊離水を発生させるも
のである。
In the first embodiment described above, free water was generated by directly mixing the liquid refrigerant with the high moisture concentration liquid in the storage chamber 8, but in this example, the high moisture concentration liquid in the storage chamber 8 was cooled. By liquefying the gas refrigerant flowing in the main stream and introducing the solution, the saturated water concentration in the liquid is lowered and free water is generated.

貯留室8の高水分濃度液を冷却する方法としては、貯留
室8の内部に、液溜め室9aより導かれた低温の冷媒を
通過させる螺旋状の冷却管9[を設置し、この冷却管9
fを通過する低温の冷媒と高水分濃度液とを熱交換させ
ることにより行う。
A method of cooling the high water concentration liquid in the storage chamber 8 is to install a spiral cooling pipe 9 inside the storage chamber 8 through which a low-temperature refrigerant guided from the liquid storage chamber 9a passes. 9
This is done by exchanging heat between the low temperature refrigerant passing through f and the high moisture concentration liquid.

従って、本実施例の遊離水発生手段9は、液溜め室9a
と冷却管9fより構成される。
Therefore, the free water generating means 9 of this embodiment has a liquid storage chamber 9a.
and a cooling pipe 9f.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図ないし第4図は本発明の第1実施例を示すもので
、第1図は水分除去装置を適用した冷凍装置の冷凍サイ
クル図、第2図水分除去装置の要部断面図、第3図は冷
媒の温度−組成面、第4図は混合モル比と混合液中の飽
和水分濃度との関係を示すグラフ、第5図および第6図
は本発明の第2実施例を示すもので、第5図は水分除去
装置を適用した冷凍装置の冷凍サイクル図、第6図は水
分除去装置の要部断面図である。 図中
1 to 4 show a first embodiment of the present invention, in which FIG. 1 is a refrigeration cycle diagram of a refrigeration system to which a moisture removal device is applied, FIG. 2 is a sectional view of main parts of the moisture removal device, and FIG. Figure 3 shows the temperature-composition aspect of the refrigerant, Figure 4 is a graph showing the relationship between the mixing molar ratio and the saturated water concentration in the liquid mixture, and Figures 5 and 6 show the second embodiment of the present invention. FIG. 5 is a refrigeration cycle diagram of a refrigeration system to which the moisture removal device is applied, and FIG. 6 is a sectional view of the main parts of the moisture removal device. In the diagram

Claims (1)

【特許請求の範囲】 1)気相の飽和水分濃度より液相の飽和水分濃度の方が
高い水分特性を有する冷媒と親水性の高い冷凍機油とを
使用する冷凍装置に適用され、(a)この冷凍装置の冷
媒蒸発器より流出した高水分濃度液を貯留する貯留室と
、 (b)この貯留室内に液冷媒を導き、この液冷媒を前記
貯留室内の高水分濃度液に溶解させることにより、前記
高水分濃度液より遊離水を発生させる遊離水発生手段と
、 (c)水分保持材を備え、発生した遊離水を前記水分保
持材に保持させる水分保持手段とから成る冷凍装置用水
分除去装置。
[Scope of Claims] 1) Applicable to a refrigeration system using a refrigerant having moisture characteristics in which the saturated moisture concentration of the liquid phase is higher than the saturated moisture concentration of the gas phase and a highly hydrophilic refrigerating machine oil, (a) A storage chamber for storing a high moisture concentration liquid flowing out from a refrigerant evaporator of this refrigeration device; , a free water generating means for generating free water from the high water concentration liquid, and (c) a water retaining means comprising a moisture retaining material and causing the generated free water to be retained in the moisture retaining material. Device.
JP16753790A 1990-06-26 1990-06-26 Moisture removing device for refrigerating device Pending JPH0455667A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16753790A JPH0455667A (en) 1990-06-26 1990-06-26 Moisture removing device for refrigerating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16753790A JPH0455667A (en) 1990-06-26 1990-06-26 Moisture removing device for refrigerating device

Publications (1)

Publication Number Publication Date
JPH0455667A true JPH0455667A (en) 1992-02-24

Family

ID=15851537

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16753790A Pending JPH0455667A (en) 1990-06-26 1990-06-26 Moisture removing device for refrigerating device

Country Status (1)

Country Link
JP (1) JPH0455667A (en)

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