JPH02287066A - Moisture-separating device for refrigeration cycle - Google Patents

Moisture-separating device for refrigeration cycle

Info

Publication number
JPH02287066A
JPH02287066A JP10810289A JP10810289A JPH02287066A JP H02287066 A JPH02287066 A JP H02287066A JP 10810289 A JP10810289 A JP 10810289A JP 10810289 A JP10810289 A JP 10810289A JP H02287066 A JPH02287066 A JP H02287066A
Authority
JP
Japan
Prior art keywords
moisture
refrigerant
refrigeration cycle
pipe
circulating
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
Application number
JP10810289A
Other languages
Japanese (ja)
Other versions
JP2767876B2 (en
Inventor
Kiyuusuke Sakakibara
久介 榊原
Keiichi Kitamura
圭一 北村
Shin Honda
伸 本田
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 JP1108102A priority Critical patent/JP2767876B2/en
Publication of JPH02287066A publication Critical patent/JPH02287066A/en
Application granted granted Critical
Publication of JP2767876B2 publication Critical patent/JP2767876B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To make moisture at all times and assuredly and exclusively separable from the refrigerant in a circulation line by providing a thin membranous material capable of allowing only moisture to permeate and to be separated from refrigerant and by providing also means for accelerating the permeation and separation. CONSTITUTION:Moisture which has entered and has been mixed with circulating refrigerant circulates in the refrigeration cycle with the refrigerant. When this condition of circulating refrigerant occurs under high pressure in a pipe 31, to a horizontal intermediate underside location of which is downwardly attached a moisture-separating device 8, only the moisture in the circulating refrigerant penetrates into the casing 70 of the moisture-separating device 8 through communicating holes in a thin metal film 62, through a moisture-permeable membrane 61, and through communicating holes in a thin metal film 63 and is absorbed by a drying agent 90, whereas the moisture-permeable membrane 61 shuts out the circulating refrigerant in the pipe 31 from permeation. Thus moisture in the refrigerant circulating in the refrigeration cycle is separated assuredly so that the cooling function and the life inherent in the refrigeration cycle can be kept unimpaired.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、冷凍サイクルに係り、特に、当該冷凍サイク
ルの冷媒循環通路の循環冷媒中の含有水分のみを分離す
るに適した水分分離装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a refrigeration cycle, and more particularly to a moisture separation device suitable for separating only moisture contained in a circulating refrigerant in a refrigerant circulation passage of the refrigeration cycle. .

(従来技術) 従来、この種の水分分離装置においては、例えば、実開
昭56−8.6472号公報に示されているように、冷
凍サイクルのエバポレータとコンプレッサとの間に接続
した配管に分岐管を設け、この分岐管に、乾燥剤を充填
した容器を組付atて、配管から分岐管を通り容器内に
流入する冷媒中の含有水分を乾燥剤により吸収するよう
にしたものがある。
(Prior art) Conventionally, in this type of water separator, a branch pipe is connected between the evaporator and the compressor of the refrigeration cycle, as shown in, for example, Japanese Utility Model Application No. 56-8.6472. There is a system in which a pipe is provided and a container filled with a desiccant is assembled into the branch pipe so that the desiccant absorbs moisture contained in the refrigerant flowing from the pipe through the branch pipe and into the container.

(発明が解決しようとする課″U) しかし、このような構成においては、容器内の乾燥剤に
はその充填に合致した水分吸収能力しかないため、冷媒
中の含有水分の吸収分離が不十分となることがある。そ
の結果、冷凍サイクルの金属部分が冷媒の含有水分に起
因し、て内部Ilv食を生じたり、或いは、膨張弁内で
の前記含有水分の氷結のためのエバポレータの冷却能力
の低下、コンプレッサの故障等を招く。
(Problem to be solved by the invention "U") However, in such a configuration, the desiccant in the container only has a moisture absorption capacity that matches the amount of water it is filled with, so the absorption and separation of the moisture contained in the refrigerant is insufficient. As a result, the metal parts of the refrigeration cycle may suffer internal ILV corrosion due to the moisture content of the refrigerant, or the cooling capacity of the evaporator may deteriorate due to the freezing of the moisture content within the expansion valve. This may lead to a decrease in air pressure and a malfunction of the compressor.

これに対しては、容器に充填すべき乾燥剤の量を増大さ
せるか、或いは充填乾燥剤の新たな乾燥剤との定期的交
換を行うことも考えられる。しかし、前者にあっては、
乾燥剤の充fX量の不必要な増大及び容器の容積の増大
を招く。また、後者にあったは、定期交換時に冷媒をも
必然的に交換しなければならないため、上述と同様に乾
燥剤の充填量の増大を余儀なくされていた。また、以上
のようなことがら乾燥剤の使用なくして冷媒の含有水分
のみの分離を実現することも望まれる。
To deal with this, it is possible to increase the amount of desiccant to be filled into the container, or to periodically replace the filled desiccant with new desiccant. However, in the former case,
This results in an unnecessary increase in the amount of desiccant fX and an increase in the volume of the container. In addition, in the latter case, the refrigerant must also be replaced during periodic replacement, which necessitates an increase in the amount of desiccant filled in the same way as described above. Further, in view of the above, it is also desired to realize separation of only the moisture contained in the refrigerant without using a desiccant.

そこで、本発明は、上述のようなことに対処すべく、冷
凍サイクルにおいてその冷媒循環通路中の冷媒からその
含有水分の″みを常に確実に分離するようにした水分分
離装置を提供しようとするものである。
Therefore, in order to deal with the above-mentioned problems, the present invention aims to provide a moisture separation device that always reliably separates only the moisture contained in the refrigerant in the refrigerant circulation path in the refrigeration cycle. It is something.

(課題を解決するための手段) かかる課題の解決にあたり、本発明の構成は、冷凍サイ
クルにおいてその冷媒循環通路の周壁の一部に形成した
開口部にこれを閉成するように組付けられて同開口部か
らの冷媒を含有水分のみの外方への透過分離を許容する
薄板状透過分離部材と、この透過分離部材の透過分離を
促進する透過分離促進手段とを備えるようにしたことに
ある。
(Means for Solving the Problems) In order to solve the problems, the configuration of the present invention is such that it is assembled into an opening formed in a part of the peripheral wall of a refrigerant circulation passage in a refrigeration cycle so as to close the opening. The present invention includes a thin plate-like permeation separation member that allows only moisture containing refrigerant to permeate and separate outward from the opening, and a permeation separation promoting means that promotes permeation separation of the permeation separation member. .

(作用効果) このように本発明を構成したことにより、前記冷媒循環
通路中の循環冷媒に水分が含有されても、この含有水分
のみが、前記透過分離促進手段の促進作用のもとに、前
記透過分離部材により外方へ容易に透過分離される。こ
のことは、かがる透過分離が、乾燥剤に不必要に依存す
ることなく、常に確実に達成されることを意味する。そ
の結果、循環冷媒からのその含有水分の常時除去が確保
されて、冷凍サイクルの本来の正常な冷却能力及び寿命
を十分に維持できる。
(Operation and Effect) By configuring the present invention in this way, even if the circulating refrigerant in the refrigerant circulation passage contains moisture, only this contained moisture is absorbed by the permeation separation promoting means. It is easily permeated and separated to the outside by the permeation separation member. This means that such permeation separation is always achieved reliably without unnecessary dependence on desiccants. As a result, the moisture contained in the circulating refrigerant is constantly removed, and the original normal cooling capacity and life of the refrigeration cycle can be sufficiently maintained.

(実施例) 以下、本発明の一実施例を図面より説明すると、第1図
及び第2図は、車両用冷凍サイクルに本発明に係る水分
分離装置Sの一例を適用した全体構成を示している。冷
凍サイクルは、コンプレッサ10を有しており、このコ
ンプレッサ10は、当該車両のエンジンにより選択的に
駆動されて、その流入冷媒を圧縮し高温高圧の圧縮冷媒
としてゴムホース11を通し配管12内に吐出する。コ
ンデンサ20は配管12からの圧縮冷媒を凝縮し配管2
1を通し凝縮冷媒としてレシーバ30内に流入させる。
(Example) Hereinafter, an example of the present invention will be explained with reference to the drawings. Figures 1 and 2 show an overall configuration in which an example of the moisture separation device S according to the present invention is applied to a refrigeration cycle for a vehicle. There is. The refrigeration cycle has a compressor 10, which is selectively driven by the engine of the vehicle, compresses the incoming refrigerant, and discharges it as a high-temperature, high-pressure compressed refrigerant into a pipe 12 through a rubber hose 11. do. The condenser 20 condenses the compressed refrigerant from the pipe 12 and transfers it to the pipe 2.
1 and flows into the receiver 30 as a condensed refrigerant.

レシーバ30は、その流入凝縮冷媒を気液分離し、液相
成分を循環冷媒として配管31を通し膨張弁40に流入
させる。膨張弁40はその流入循環冷媒をその開度に応
じ膨張させて配管41を通しエバポレータ50内に流入
させる。エバポレータ50は、その流入冷媒に応じ被冷
却媒体を冷却するとともに、同流入冷媒を配管51及び
ゴムホース52を通しコンプレッサ1oに流入させる。
The receiver 30 separates the incoming condensed refrigerant into gas and liquid, and causes the liquid phase component to flow into the expansion valve 40 through the pipe 31 as a circulating refrigerant. The expansion valve 40 expands the inflow circulating refrigerant according to its opening degree and causes it to flow into the evaporator 50 through the pipe 41. The evaporator 50 cools the medium to be cooled according to the inflowing refrigerant, and causes the inflowing refrigerant to flow into the compressor 1o through a pipe 51 and a rubber hose 52.

水分分離装置Sは、第1図及び第2図に示すごとく、配
管31の水平状中間部位の外壁下側部に垂下状に組付け
られている。この水分分離装置Sは、第2図に示すごと
く、三層状重合薄板体6゜を有しており、この重合薄板
体6oは、配管31の前記外壁下側部に下方に向は突出
形成してなる環状開口部32の内周壁に形成した環状溝
部32a内に、その外周縁部を嵌着し、開口部32にこ
れを閉成するように組付けられている。
As shown in FIGS. 1 and 2, the moisture separator S is attached to the lower side of the outer wall of the horizontal intermediate portion of the pipe 31 in a hanging manner. As shown in FIG. 2, this moisture separator S has a three-layer polymeric thin plate body 6°, and this polymeric thin plate body 6o is formed on the lower side of the outer wall of the pipe 31 so as to protrude downward. The outer circumferential edge portion thereof is fitted into an annular groove portion 32a formed in the inner circumferential wall of an annular opening portion 32, and the opening portion 32 is assembled in such a manner that the groove portion 32a is closed.

重合薄板体60は、水分透過膜61にその上下表面側か
ら金属薄板62.63をそれぞれ重合して構成(第1図
及び第3図参照)してなるもので、水分透過膜61は、
冷媒中の含有水分のみに対し良好な透水性を有するポリ
イミド膜(板厚50(μm)程度)によって形成されて
いる。金属薄板62は、第3図に示すように、複数の連
通孔62a〜62aを離散状に穿設して形成されており
、一方、金属薄板63は、複数の連通孔63a〜63a
を複数の連通孔62a〜62aに対し水分透過膜61を
介しそれぞれ同一形状にて対向している。かかる場合、
両金属薄板62.63は、その各弾力により、水分透過
[61を、外圧とはががわりなく、上下方向に変形しな
いように補強する役割を果す。
The polymerized thin plate body 60 is constructed by superposing thin metal plates 62 and 63 on a water permeable membrane 61 from its upper and lower surfaces (see FIGS. 1 and 3).
It is formed of a polyimide membrane (about 50 (μm) thick) that has good water permeability only to the water contained in the refrigerant. As shown in FIG. 3, the thin metal plate 62 is formed by drilling a plurality of communicating holes 62a to 62a in a discrete manner, while the thin metal plate 63 has a plurality of communicating holes 63a to 63a.
are opposed to the plurality of communication holes 62a to 62a with the same shape, respectively, with the moisture permeable membrane 61 interposed therebetween. In such case,
Both thin metal plates 62 and 63 play the role of reinforcing the moisture permeation [61] so as not to be deformed in the vertical direction regardless of external pressure due to their respective elasticities.

また、水分分離袋Wsは、第1図にて図示断面形状を有
するケーシング70を有しており、このケーシング70
は、その大径開口部71を配管31の開口部32に上下
及び外方がら締着して組付けられている。また、0リン
グ8oがケーシング70の段部と開口部32の端面との
間にてケーシング70の開1−]部32への締着により
押圧介装されており、このOリング80は、ケーシング
70の小径部内に収容した乾燥剤90を外部からシール
する。
Further, the moisture separation bag Ws has a casing 70 having the cross-sectional shape shown in FIG.
is assembled with its large diameter opening 71 fastened to the opening 32 of the pipe 31 from above and below and from the outside. Further, an O-ring 8o is press-inserted between the stepped portion of the casing 70 and the end face of the opening 32 by fastening to the opening 1-] portion 32 of the casing 70. The desiccant 90 housed in the small diameter portion of the 70 is sealed from the outside.

以トのように構成した本実施例において、当該重両のエ
ンジンの始動のもとにコンプレッサ10が駆動されれば
、同=lンブレッサ10がその流入冷媒を圧縮し高温高
圧の圧縮冷媒としてゴムポース11を通し配管12内に
吐出する。づ−ると、この配管12からの圧縮冷媒が、
コンデンサ20により凝縮さノじC凝縮冷媒として配管
21を通りレシーバ30内に流入して気液分離される。
In this embodiment configured as described above, when the compressor 10 is driven when the engine of the heavy vehicle is started, the compressor 10 compresses the incoming refrigerant and converts it into a high-temperature, high-pressure compressed refrigerant into a rubber port. 11 and is discharged into piping 12. In other words, the compressed refrigerant from this pipe 12 is
The refrigerant is condensed by the condenser 20 and flows into the receiver 30 through the pipe 21, where it is separated into gas and liquid.

ついで、レジーバ30からグ)液相成分のみが循環冷媒
として配管31を通り膨張弁40に流入し、て膨張され
低温低圧の冷媒として配管41を通りエバポレータ50
に流入ずイ)。このため、エバポレータ50がその流入
冷媒に応じ被冷却媒体を冷却するとともに同冷媒を配管
51及びゴムホース52を通りコンプレッサ]0に流入
する。
Then, only the liquid phase component from the reservoir 30 flows into the expansion valve 40 through the piping 31 as a circulating refrigerant, is expanded, and passes through the piping 41 as a low-temperature, low-pressure refrigerant into the evaporator 50.
(a). Therefore, the evaporator 50 cools the medium to be cooled according to the inflowing refrigerant, and the refrigerant flows into the compressor 0 through the pipe 51 and the rubber hose 52.

このような冷凍サイクルにおける冷媒の循環過程におい
て、各ゴムホース11.52内にそσ)周壁を通り外方
から水分が侵入したり、成り)は各配管12.21,3
1.41及び51或いは各ゴムホース11.52の接続
端部から各配管酸l/)(ま各ゴムホース内に水分が侵
入したりして、この水分が循環冷媒に混入しこれと共に
冷凍サイクルを循環するようになったものとする。
During the refrigerant circulation process in such a refrigeration cycle, moisture may enter into each rubber hose 11.52 from the outside through the peripheral wall,
1.41 and 51 or from the connecting end of each rubber hose 11.52 each piping acid l/) (Moisture may enter into each rubber hose, and this moisture mixes with the circulating refrigerant and circulates in the refrigeration cycle with it. It is assumed that the

このような状態においては、配管31内の状態冷媒が高
圧であり、かつ水分分離袋ZSが配管31の水平状中間
部位から下方へ垂下しているため、配管31内の循環冷
媒が水分透過膜61によりその透過を阻止された状態に
て、同循環冷媒中の水分のみが金属薄板62の連通孔6
2a、水分透過膜61及び金属薄板63の各連通孔63
 aを通りケーシング70内に侵入し乾燥剤90により
吸収される。従って、冷凍サイクル中の循環冷媒からの
含有水分の分離が確実に行なわれるので、冷凍サイクル
本来の冷却機能及び寿命を確保できる。
In such a state, the refrigerant in the pipe 31 is at high pressure and the moisture separation bag ZS hangs downward from the horizontal middle part of the pipe 31, so the circulating refrigerant in the pipe 31 is not absorbed by the moisture permeable membrane. 61, only the moisture in the circulating refrigerant flows through the communication hole 6 of the thin metal plate 62.
2a, each communication hole 63 of the moisture permeable membrane 61 and the thin metal plate 63
a and enters the casing 70 and is absorbed by the desiccant 90. Therefore, since the moisture contained in the circulating refrigerant in the refrigeration cycle is reliably separated, the original cooling function and service life of the refrigeration cycle can be ensured.

かかる場合、水分透過膜61が両金属薄板62゜63に
よりその弾力でもって挟持されているので、水分透過膜
6]が循環冷媒の圧力でも−、てr゛方ノ\たわむこと
はない。
In this case, since the moisture permeable membrane 61 is held between the two thin metal plates 62 and 63 by their elasticity, the moisture permeable membrane 6 does not bend even under the pressure of the circulating refrigerant.

Jた、乾燥剤(90の交換にあな・−)ては、二1ンー
ノ・レッザ1(−)の停止下にて、ケーシング70の開
口部32どの締着を解除して同ゲージング70を開1−
1部゛32から開放し、新たな乾燥剤をゲージング70
内に収容し、た−1.で同ケーシング70を再び開1−
1部′32に(1)リング80を介し7−1−述と同様
に締着ずれはよいり〕で、乾燥剤の交換時に冷凍サイク
ルの循環冷媒をも交換し、なければならないというよう
な不都合も確実に解消される。また、乾燥剤の交換はL
述のような簡単な作業で行ない得るの”ζ、ケーシング
70の収容乾燥剤の址は必要鼓小眼に抑制できる。また
、水分分離装置Sを組付は人=配管31内の冷媒は上述
のように高温高圧であるため、同冷媒中の水蒸気圧が高
い。従って、2F述のような4<分の分離が迅速に達成
され得る。なお、0リング80のシール機能のため、外
部の水分がケーシング70内に侵入することらない。
For the desiccant (90), remove the fastening of the opening 32 of the casing 70 and open the gauging 70 while the 21st Reza 1 (-) is stopped. 1-
Release the first part from 32 and gage new desiccant at 70.
-1. Open the casing 70 again with 1-
Part 1'32 states that (1) The ring 80 should be tightened in the same manner as described in 7-1. Any inconvenience will definitely be resolved. Also, when replacing the desiccant,
This can be done with a simple operation as described above, and the amount of desiccant stored in the casing 70 can be kept to a small amount.Moreover, the moisture separator S can be assembled by a person, and the refrigerant in the pipe 31 can be refrigerated as described above. Since the refrigerant is at high temperature and high pressure, the water vapor pressure in the refrigerant is high.Therefore, the separation of 4< minutes as described in 2F can be quickly achieved.In addition, due to the sealing function of the O-ring 80, the water vapor pressure in the refrigerant is high. Moisture does not enter into the casing 70.

次に、面層実施例の変形例について第71図を参照して
説明すると、この変形例においζは、水分分離装置Sa
が、助層実施例にて述べた水分分離装置Sに代えて、ゴ
ムポース]1の近傍の配管12の水平状中間部位の外壁
下側部に垂下状に組付けられている。この水分分離装置
Saにおいては、助層実施例にて述べたケーシング70
を、配管12の前記外壁F側部に向は突出形成しζなる
環状開口部1.2 aに下方及び外方から締着して組付
け、前記実施例にて述べた水分透過膜61及び金属薄板
62を、ケーシング70の段部と開!−1部]、 2 
aの端面との間にて0リング80を介し7ケーシング7
0の開口部12aへの締着により押圧介装し、配管51
の中間部位を第4図に示ずごとくゲージング70の小径
部内にU字状に気密的に貫通させ、ケーシング70の小
径部の内部を排水管72により外部に開放し、かつ乾燥
剤90を省略するように構成されている。なお、排水管
72は外部からの水分の侵入を阻止すべく屈曲形成され
ている。
Next, a modification of the surface layer embodiment will be explained with reference to FIG. 71. In this modification, ζ is the water separator Sa
However, in place of the moisture separator S described in the auxiliary layer embodiment, it is installed in a hanging manner on the lower side of the outer wall of the horizontal intermediate portion of the pipe 12 near the rubber port 1. In this moisture separator Sa, the casing 70 described in the auxiliary layer embodiment
is assembled into the annular opening 1.2a projecting from the side of the outer wall F of the piping 12 and fastened from below and from the outside, and the moisture permeable membrane 61 and Open the metal thin plate 62 to the step part of the casing 70! -1 copy], 2
7 casing 7 via the O ring 80 between the end face of a
0 to the opening 12a, and the piping 51
The intermediate portion of the casing 70 is passed through the small diameter portion of the gauging 70 airtightly in a U-shape as shown in FIG. is configured to do so. Note that the drain pipe 72 is bent to prevent moisture from entering from the outside.

このように構成した本変形例においては、配管51内の
冷媒が低温であること、及びケーシング70の小径部内
の飽和水蒸気圧が同冷媒の低温のため同温度の飽和蒸気
圧(例えば、10°Cで92rnm)−1g)以丁に抑
制されることに基き、水分透過膜61の)、’jiに比
べ下方の方か水蒸気圧が低くなる。このため、かかる水
蒸気圧差に起因して配管12内の冷媒中の水分の水分透
過膜6】を介するケーシング70の小fR部への透過分
離が効率よく行なわれる。従って、乾燥剤90に依存す
ることなく冷凍サイクルの循環冷媒の含有水分を分離で
きる。
In this modified example configured in this way, the refrigerant in the pipe 51 is at a low temperature, and the saturated vapor pressure in the small diameter portion of the casing 70 is low, so the saturated vapor pressure at the same temperature (for example, 10° Based on the fact that the water vapor pressure is suppressed to 92rnm)-1g) at C, the water vapor pressure is lower in the lower part than in ) and 'ji of the moisture permeable membrane 61. Therefore, due to this water vapor pressure difference, the moisture in the refrigerant in the pipe 12 is efficiently permeated and separated into the small fR portion of the casing 70 via the moisture permeable membrane 6. Therefore, the moisture contained in the circulating refrigerant of the refrigeration cycle can be separated without depending on the desiccant 90.

また、この変形例において、ケーシング70内への配管
51の貫通を省略するとともに、ケーシング70の小径
部から第5図に示すごとく吸引ロア3を延出させて、こ
の吸引ロア3を介しケーシング70の小径部内にエンジ
ンの負圧を付与するようにしてL述のような水蒸気圧差
を形成するようにし、でも実質的に同様の作用効果を達
成できる。
In addition, in this modification, the passage of the pipe 51 into the casing 70 is omitted, and the suction lower 3 is extended from the small diameter portion of the casing 70 as shown in FIG. Even if negative pressure of the engine is applied to the small diameter portion of the engine to form a water vapor pressure difference as described in L, substantially the same effect can be achieved.

第1図は本発明の一実施例を示づ拡大[!Ji曲図、第
2図は本発明を適用した冷凍サイクルの概略図、第3図
は第1図の本発明の要部拡大斜iJ1図、第、・1図は
前記実施例の部分的変形例を示す断面[’21、及び第
5図は同地の変形例を示す断面図である。
FIG. 1 shows an embodiment of the present invention and is enlarged [! Fig. 2 is a schematic diagram of a refrigeration cycle to which the present invention is applied; Fig. 3 is an enlarged oblique view of the main part of the present invention in Fig. 1; Fig. 1 is a partial modification of the above embodiment. A cross section showing an example ['21] and FIG. 5 are cross-sectional views showing a modification of the same area.

符  号  の  説  明 10・・・コンプレッサ、11.52・・・ゴムポース
、12,21.3]、、41.51・・・配管、12a
、32・・・開口部、30  ・レシーバ、40・・・
膨張弁、50・ ・エバポレータ、61・・・水分透過
膜、62.63・・ 金属薄板、70・・・ケーシング
、72・・・排水管、73・・・吸引口、S、Sa・ 
・水分分離装置。
Explanation of symbols 10...Compressor, 11.52...Rubber port, 12, 21.3], 41.51...Piping, 12a
, 32... opening, 30 - receiver, 40...
Expansion valve, 50... Evaporator, 61... Moisture permeable membrane, 62.63... Metal thin plate, 70... Casing, 72... Drain pipe, 73... Suction port, S, Sa...
・Water separation device.

Claims (1)

【特許請求の範囲】[Claims]  冷凍サイクルにおいてその冷媒循環通路の周壁の一部
に形成した開口部にこれを閉成するように組付けられて
同開口部からの冷媒の含有水分のみの外方への透過分離
を許容する薄板状透過分離部材と、この透過分離部材の
透過分離を促進する透過分離促進手段とを備えてなる冷
凍サイクルのための水分分離装置。
A thin plate that is assembled to close an opening formed in a part of the peripheral wall of a refrigerant circulation passage in a refrigeration cycle and allows only moisture contained in the refrigerant to permeate and separate outward from the opening. A moisture separation device for a refrigeration cycle, comprising a permeation separation member and permeation separation promoting means for promoting permeation separation of the permeation separation member.
JP1108102A 1989-04-27 1989-04-27 Moisture separator for refrigeration cycle Expired - Lifetime JP2767876B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1108102A JP2767876B2 (en) 1989-04-27 1989-04-27 Moisture separator for refrigeration cycle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1108102A JP2767876B2 (en) 1989-04-27 1989-04-27 Moisture separator for refrigeration cycle

Publications (2)

Publication Number Publication Date
JPH02287066A true JPH02287066A (en) 1990-11-27
JP2767876B2 JP2767876B2 (en) 1998-06-18

Family

ID=14475926

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1108102A Expired - Lifetime JP2767876B2 (en) 1989-04-27 1989-04-27 Moisture separator for refrigeration cycle

Country Status (1)

Country Link
JP (1) JP2767876B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5301520A (en) * 1991-04-15 1994-04-12 Nippondenso Co., Ltd. Water removing device in refrigerating system
EP1233242A2 (en) * 1996-02-09 2002-08-21 Matsushita Electric Industrial Co., Ltd. Air conditioner
EP1363088A1 (en) * 2002-05-08 2003-11-19 SKG Italiana S.P.A. Receiver drier

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5686472U (en) * 1979-12-06 1981-07-11
JPS63123965A (en) * 1986-11-14 1988-05-27 株式会社日立製作所 Drier for refrigeration cycle

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5686472U (en) * 1979-12-06 1981-07-11
JPS63123965A (en) * 1986-11-14 1988-05-27 株式会社日立製作所 Drier for refrigeration cycle

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5301520A (en) * 1991-04-15 1994-04-12 Nippondenso Co., Ltd. Water removing device in refrigerating system
US5490397A (en) * 1991-04-15 1996-02-13 Nippondenso Co., Ltd. Water removing device in refrigerating system
DE4212367C2 (en) * 1991-04-15 2000-08-03 Denso Corp Device for removing water in a cooling system
EP1233242A2 (en) * 1996-02-09 2002-08-21 Matsushita Electric Industrial Co., Ltd. Air conditioner
EP1233242A3 (en) * 1996-02-09 2002-09-04 Matsushita Electric Industrial Co., Ltd. Air conditioner
EP1363088A1 (en) * 2002-05-08 2003-11-19 SKG Italiana S.P.A. Receiver drier

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