JPH0440136Y2 - - Google Patents

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Publication number
JPH0440136Y2
JPH0440136Y2 JP1987111366U JP11136687U JPH0440136Y2 JP H0440136 Y2 JPH0440136 Y2 JP H0440136Y2 JP 1987111366 U JP1987111366 U JP 1987111366U JP 11136687 U JP11136687 U JP 11136687U JP H0440136 Y2 JPH0440136 Y2 JP H0440136Y2
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JP
Japan
Prior art keywords
water
refrigerant
oil
heat exchanger
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.)
Expired
Application number
JP1987111366U
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Japanese (ja)
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JPS6416572U (en
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Publication date
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Priority to JP1987111366U priority Critical patent/JPH0440136Y2/ja
Publication of JPS6416572U publication Critical patent/JPS6416572U/ja
Application granted granted Critical
Publication of JPH0440136Y2 publication Critical patent/JPH0440136Y2/ja
Expired legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【考案の詳細な説明】 「産業上の利用分野」 本考案は、冷凍サイクルの低圧部に混入して細
氷となつた水分をも確実に捕捉し得る水、油等の
分離除去装置に係り、特に冷凍サイクルの低圧部
が真空状態となるような極定温度の冷却サイクル
に好適に使用される水分除去装置に関する。
[Detailed description of the invention] "Industrial application field" This invention relates to a device for separating and removing water, oil, etc., which can reliably capture water that has entered the low-pressure section of a refrigeration cycle and turned into fine ice. In particular, the present invention relates to a moisture removal device suitable for use in extremely constant temperature cooling cycles where the low pressure section of the refrigeration cycle is in a vacuum state.

「従来の技術」 一般に冷媒を用いる冷凍サイクル特にフロン系
冷媒を使用した装置においては水分を嫌い、又該
冷凍サイクルを構成する各種機器の腐食の点から
も水分はない方が良いが、長期間冷却装置を運転
しているとメンテナンスその他の理由により装置
内への水分が混入する場合が多々ある。
"Prior Art" Generally, refrigeration cycles that use refrigerants, particularly equipment that uses fluorocarbon-based refrigerants, do not like moisture, and it is better to avoid moisture for a long period of time in order to prevent corrosion of the various devices that make up the refrigeration cycle. When operating a cooling system, moisture often enters the system due to maintenance or other reasons.

通常、冷却装置の水分除去は凝縮器又は受液器
出口に設けたドライヤー(乾燥器)により行なわ
れているが、低圧部の特に0℃以下の領域に於い
ては水分が氷となつて装置内壁面に付着するか、
冷媒の中に細氷となつて混入するので、かかる氷
化した水分は、低圧部で除去しない限りそのまま
冷却サイクル中に残留してしまい、特に長時間連
続運転される冷却装置では徐々に前記細氷が累積
して増加し、前記冷媒中に一定以上前記細氷が混
入する事により、装置内の各所で細氷が滞留した
り又装置内壁面に一定厚み以上付着して、運転を
継続することが不可能となる場合もある。
Normally, water removal from cooling equipment is carried out by a dryer installed at the outlet of the condenser or liquid receiver, but in low-pressure areas, especially in areas below 0°C, water turns into ice and Does it adhere to the inner wall surface?
Since the frozen water is mixed into the refrigerant as fine ice, it will remain in the cooling cycle unless it is removed in the low-pressure section. Especially in a cooling system that is operated continuously for a long time, the frozen water will gradually disappear. As the ice accumulates and more than a certain amount of ice gets mixed into the refrigerant, the ice accumulates in various places in the device or adheres to the inner wall of the device to a certain thickness or more, causing the operation to continue. There are times when this is not possible.

この為一般的な冷却装置では前記低圧部に連結
した油溜器に取付けた排出弁により油分と一緒に
前記細氷化した水分も排出するように構成したも
のが多い。
For this reason, many common cooling devices are constructed so that the finely frozen water is also discharged together with the oil through a discharge valve attached to an oil sump connected to the low pressure section.

即ち油溜器を使用して油を抜くには、先ず低圧
部より冷媒、油分及び細氷を含む水分の混合液を
油溜器を貯溜させ、これを油溜器に具備されたヒ
ーター(加熱器)で加熱して冷媒を蒸発させた
後、その蒸発した冷媒を冷凍サイクルの低圧部側
に戻入させることにより油溜器に油分と水分を残
留させて、その残留分を排出するという方法で行
なつている。
In other words, to remove oil using an oil sump, first store a mixture of water containing refrigerant, oil, and thin ice in the oil sump from the low-pressure part, and then use the heater (heating After evaporating the refrigerant by heating the refrigerant in the refrigeration cycle, the evaporated refrigerant is returned to the low-pressure side of the refrigeration cycle, leaving oil and moisture in the oil sump and discharging the remaining amount. I am doing it.

しかしながら、低圧部が真空状態となるような
極低温度の冷凍サイクルにおいては、油溜器を加
熱すると水の蒸気分圧の関係で冷媒と共に水分も
蒸発してしまい、該蒸発した水分が再度冷凍サイ
クル内に混入し凝結し、弁、管部を閉塞する弊害
が生じ、前記水分を完全に除去する事が不可能で
あつた。
However, in extremely low temperature refrigeration cycles where the low pressure section is in a vacuum state, when the oil sump is heated, water evaporates together with the refrigerant due to the water vapor partial pressure, and the evaporated water is refrigerated. The water gets mixed into the cycle and condenses, causing problems such as clogging valves and pipes, making it impossible to completely remove the water.

本考案はかかる従来技術の欠点に鑑み、低圧部
が真空状態となるような極低温度の冷凍サイクル
においても、油分と併せ前記細氷化した水分を完
全に除去し得る水、油等の分離除去装置を提供す
る事を目的とする。
In view of the shortcomings of the prior art, the present invention has been developed to separate water, oil, etc., which can completely remove the finely frozen water together with oil even in extremely low temperature refrigeration cycles where the low pressure section is in a vacuum state. The purpose is to provide a removal device.

「問題点を解決しようとする手段」 本考案はかかる技術的課題を達成する為に、 冷媒、油分及び細氷を含む水分の混合液を貯
溜する容器1底部に加熱手段2を設けた点、そ
して該加熱手段2が、前記混合液を水の蒸発温
度以上に加熱する加熱手段である点 前記加熱手段2の混合液貯溜位置より上方空
間位置に、冷却サイクルの低圧冷媒、より具体
的には水の凍結点以下の温度を有する冷媒を導
通する熱交換器3を設けた点 前記混合液を加熱手段2により加熱した後、
該混合液中の蒸発水分を熱交換器3に霜として
付着させた後の冷媒ガスを熱交換器3上方に設
けた管路9を介して冷凍サイクル低圧部側に導
入可能に構成した点 を必須構成要件とする水、油等の分離除去装置を
提案する。
"Means for Solving Problems" In order to achieve the technical problem, the present invention has the following points: A heating means 2 is provided at the bottom of a container 1 that stores a liquid mixture of water containing a refrigerant, oil, and fine ice. The heating means 2 is a heating means that heats the liquid mixture to a temperature higher than the evaporation temperature of water.The low-pressure refrigerant of the cooling cycle, more specifically, is placed in a space above the liquid mixture storage position of the heating means 2. A heat exchanger 3 is provided that conducts a refrigerant having a temperature below the freezing point of water.After the mixed liquid is heated by the heating means 2,
The refrigerant gas after the evaporated water in the liquid mixture has been deposited as frost on the heat exchanger 3 can be introduced into the low pressure section of the refrigeration cycle through the pipe 9 provided above the heat exchanger 3. We propose a separation and removal device for water, oil, etc. as an essential component.

「作用」 例えば、前記容器1を極低温冷凍サイクルの低
圧部10(ローレシーバ)に連結した場合、該低
圧部内の0℃以下の低温度域で氷細となつて残留
している水分を冷媒、油分とともに貯溜容器1側
に取り出した後、これを容器1底部に位置する加
熱手段2により加熱して前記細氷を融解させ、冷
媒とともに蒸発させる。
"Function" For example, when the container 1 is connected to the low pressure section 10 (low receiver) of a cryogenic refrigeration cycle, the ice becomes fine in the low temperature range of 0°C or less in the low pressure section and the remaining water is removed by the refrigerant. After taking it out to the storage container 1 side together with the oil, it is heated by the heating means 2 located at the bottom of the container 1 to melt the thin ice and evaporate it together with the refrigerant.

そして前記冷媒及び水蒸気の混合気体は、容器
1内に設けた前記熱交換器3と接触する事によ
り、再び前記混合気体が冷却され、水蒸気のみが
氷結されて熱交換器3のコイル3aに付着し、該
熱交換器3により水分が除去された冷媒ガスのみ
が、管路9を介して冷却サイクル低圧部側に導入
される。
The mixed gas of the refrigerant and water vapor then comes into contact with the heat exchanger 3 provided in the container 1, whereby the mixed gas is cooled again, and only the water vapor is frozen and adheres to the coil 3a of the heat exchanger 3. However, only the refrigerant gas from which moisture has been removed by the heat exchanger 3 is introduced into the low-pressure part side of the cooling cycle via the pipe line 9.

そして熱交換器3のコイル3aに付着した氷結
水分は、デフロスト又はホツトガス等を利用して
溶融させて、容器1底側に落下させて該底側に滞
留している油分とともに又は単独で外部に排出さ
せる。
The frozen moisture adhering to the coil 3a of the heat exchanger 3 is melted using defrost or hot gas, and is allowed to fall to the bottom side of the container 1 and released to the outside together with the oil remaining on the bottom side or alone. Let it drain.

これにより、前記加熱手段2により蒸発した水
分を熱交換器3により完全に捕捉する事が出来る
為に、該水分が再度冷凍サイクル内に混入し凝結
する恐れを除去し、低圧部が真空状態となるよう
な極低温度の冷凍サイクルにおいても容易に細氷
化した水分確実に除去する事が可能である。
As a result, the moisture evaporated by the heating means 2 can be completely captured by the heat exchanger 3, thereby eliminating the risk of the moisture entering the refrigeration cycle again and condensing, and keeping the low pressure section in a vacuum state. Even in extremely low-temperature refrigeration cycles, it is possible to easily and reliably remove water that has turned into fine ice.

尚本考案は冷媒を用いた冷凍サイクルであれ
ば、極低温度の冷却サイクル以外にも容易に適用
可能である。
It should be noted that the present invention can be easily applied to refrigeration cycles that use refrigerants other than extremely low temperature refrigeration cycles.

「実施例」 以下、図面を参照して本考案の好適な実施例を
例示的に詳しく説明する。但しこの実施例に記載
されている構成部品の寸法、材質、形状、その相
対配置などは特に特定的な記載がない限りは、こ
の考案の範囲をそれのみに限定する趣旨ではな
く、単なる説明例に過ぎない。
Embodiments Hereinafter, preferred embodiments of the present invention will be described in detail by way of example with reference to the drawings. However, unless otherwise specified, the dimensions, materials, shapes, and relative positions of the components described in this example are not intended to limit the scope of this invention, but are merely illustrative examples. It's nothing more than that.

図面は、冷凍サイクルの低圧部であるローレシ
ーバ10(低圧液溜)より取り出した冷媒、油分
及び細氷を含む水分の混合液より水及び油を分離
除去し、冷媒のみを冷却サイクルの低圧側に戻入
する、本考案に実施例に係る分離除去装置を示
す。
The drawing shows that water and oil are separated and removed from a mixture of refrigerant, oil, and water containing thin ice taken out from the low-pressure receiver 10 (low-pressure liquid reservoir), which is the low-pressure part of the refrigeration cycle, and only the refrigerant is transferred to the low-pressure side of the refrigeration cycle. 1 shows a separation and removal device according to an embodiment of the present invention, which is returned to a container.

図中1は、前記混合液を貯溜する為に直立配置
された円筒状容器で、ローレシーバ10に貯溜さ
れた前記混合液を導管5及び調整弁6を介して、
その中腹部より容器1内に取り出し可能に構成し
ている。
In the figure, reference numeral 1 denotes a cylindrical container arranged upright to store the mixed liquid, and the mixed liquid stored in the low receiver 10 is passed through a conduit 5 and a regulating valve 6.
It is constructed so that it can be taken out into the container 1 from its midsection.

又前記容器1は、底側に排出弁7を、又容器1
内底側位置にヒータ2を、中腹部より上方域にコ
イル状熱交換器3を、更に該熱交換器3と対面す
る位置にホツトガス導出口13を、そして更に容
器1頂部に冷媒戻管9を夫々設けている。次にか
かる各種部材について詳細に説明する。
Further, the container 1 has a discharge valve 7 on the bottom side, and a discharge valve 7 on the bottom side.
A heater 2 is installed at the inner bottom side, a coiled heat exchanger 3 is installed above the midsection, a hot gas outlet 13 is installed at a position facing the heat exchanger 3, and a refrigerant return pipe 9 is installed at the top of the container 1. are set up respectively. Next, the various members will be explained in detail.

加熱ヒータ2は容器1内に貯溜された混合液を
加熱し、その加熱温度を、少なくとも細氷を融解
させ且つ冷媒を蒸発するに足るだけの温度に設定
する。
The heater 2 heats the liquid mixture stored in the container 1, and sets the heating temperature to a temperature sufficient to melt at least the thin ice and evaporate the refrigerant.

コイル状熱交換器3はローレシーバ10と冷凍
機11間を連結する導管20を分岐する分岐管8
と連通し、冷凍サイクルの低圧側に吸入可能に構
成するとともに、該コイル状熱交換器3により容
器1内で熱交換された冷媒は分岐管8、導管2
0、冷凍機11、蒸発器12、ローレシーバ1
0、ポンプ18、導管14及び調整弁15を介し
て熱交換器3側に循環されるよう構成している。
The coiled heat exchanger 3 has a branch pipe 8 that branches a conduit 20 connecting the low receiver 10 and the refrigerator 11.
The refrigerant that has been heat exchanged in the container 1 by the coiled heat exchanger 3 is connected to the branch pipe 8 and the conduit 2.
0, refrigerator 11, evaporator 12, low receiver 1
0, pump 18, conduit 14 and regulating valve 15 to be circulated to the heat exchanger 3 side.

ホツトガス導出口13は導管17を介して圧縮
機の吐出側その他のホツトガス源(図示せず)と
連通させ、熱交換器3の冷却コイル3aに氷結し
た水分を融解可能に構成する。
The hot gas outlet 13 is connected to the discharge side of the compressor and other hot gas sources (not shown) via a conduit 17, and is configured to be able to melt water frozen in the cooling coil 3a of the heat exchanger 3.

容器1頂部に設けた冷媒戻管9は、調整弁16
を介してローレシーバ10と蒸発器11間を連結
する導管20と連接している。
A refrigerant return pipe 9 provided at the top of the container 1 is connected to a regulating valve 16.
It is connected to a conduit 20 that connects the low receiver 10 and the evaporator 11 via a pipe.

次にかかる構成に基づく作用を説明する。 Next, the operation based on this configuration will be explained.

ローレシーバ10に滞留した冷媒の内、上層に
位置する部分は、油分及び細氷を含む混合液とな
つている為に、これを導管5及び調整弁6を介し
て容器1内に送り出す。
The upper layer of the refrigerant retained in the low receiver 10 is a liquid mixture containing oil and thin ice, and is sent into the container 1 via the conduit 5 and the regulating valve 6.

容器1内に貯溜された混合液はヒータ2により
加熱され、水分を含む冷媒を蒸発させる。そして
該含水冷媒が、熱交換器3のコイル3aに接触す
ると、冷却されて水分のみが熱交換器3の冷却コ
イル3aに氷結し、容器1頂部より冷媒のみを冷
媒戻管9及び調整弁16を介して低圧導管20側
に戻入し、ローレシーバ10を通過して他の冷媒
とともに冷凍機11に吸入させることができる。
The mixed liquid stored in the container 1 is heated by the heater 2 to evaporate the refrigerant containing water. When the water-containing refrigerant contacts the coil 3a of the heat exchanger 3, it is cooled and only moisture freezes on the cooling coil 3a of the heat exchanger 3, and only the refrigerant is sent from the top of the container 1 to the refrigerant return pipe 9 and the regulating valve 16. The refrigerant can be returned to the low-pressure conduit 20 side through the low-pressure conduit 20, pass through the low receiver 10, and be sucked into the refrigerator 11 together with other refrigerants.

一方熱交換器3の冷却コイル3aに所定量以上
の水分が氷結した場合は、前記ヒータ2の加熱を
停止するとともに、熱交換器3内へ低圧冷媒の供
給を停止言い変えれば冷却コイル3aの冷却を停
止した後、導出口より圧縮機からのホツトガスを
放出して前記冷却コイル3aに氷結した水分を溶
解して油分と一緒に排出弁7より排出する。
On the other hand, if a predetermined amount or more of water freezes in the cooling coil 3a of the heat exchanger 3, the heating of the heater 2 is stopped, and the supply of low-pressure refrigerant into the heat exchanger 3 is stopped.In other words, the cooling coil 3a is stopped. After cooling is stopped, the hot gas from the compressor is discharged from the outlet to dissolve the water frozen in the cooling coil 3a and discharged from the discharge valve 7 together with the oil.

尚、油分が無くとも同様の結果が得られる。 Note that similar results can be obtained even without oil.

かかる実施例によれば本考案の効果を円滑に達
成出来る。
According to such an embodiment, the effects of the present invention can be smoothly achieved.

尚、図中18はローレシーバ10内の冷媒液を
循環させるポンプ、21はレベルスイツチ、22
は圧力計 23は安全弁である。
In addition, in the figure, 18 is a pump that circulates the refrigerant liquid in the low receiver 10, 21 is a level switch, and 22
is a pressure gauge and 23 is a safety valve.

「効果」 以上記載した如く本考案によれば、簡単な構成
にて低圧部が真空状態となるような極低温度の冷
却サイクルにおいても、油分と併せ前記細氷化し
た水分を完全に除去する事が出来る。等の種々の
著効を有す。
"Effects" As described above, according to the present invention, even in an extremely low temperature cooling cycle where the low pressure part is in a vacuum state with a simple configuration, the finely frozen water can be completely removed together with the oil. I can do things. It has various effects such as

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

図面は冷却サイクルの低圧部に混入した水分を
除去する本考案の実施例に係る装置の概略説明図
である。 10……ローレシーバ、2……加熱手段、3…
…熱交換器、1……容器。
The drawing is a schematic explanatory diagram of an apparatus according to an embodiment of the present invention for removing moisture mixed in a low-pressure part of a cooling cycle. 10...Low receiver, 2...Heating means, 3...
...Heat exchanger, 1... Container.

Claims (1)

【実用新案登録請求の範囲】 冷凍サイクル中に組込まれる水、油等の分離除
去装置において、 冷媒、油分及び細氷を含む水分の混合液を貯溜
する容器底部に設けられ、前記混合液を水の蒸発
温度以上に加熱する加熱手段の混合液貯溜位置よ
り上方空間位置に、水の凍結点以下の温度を有す
る冷媒を導通する熱交換器を設け、 前記混合液を加熱手段により加熱した後、該混
合液中の蒸発水分を熱交換器に霜として付着させ
た後の冷媒ガスを熱交換器上方に設けた管路を介
して冷凍サイクル低圧部側に導入可能に構成した
ことを特徴とする冷凍サイクル中に組込まれる
水、油等の分離除去装置。
[Claims for Utility Model Registration] In a device for separating and removing water, oil, etc., which is incorporated into a refrigeration cycle, the device is provided at the bottom of a container that stores a liquid mixture of water containing a refrigerant, oil, and fine ice, and the liquid mixture is separated into water. A heat exchanger that conducts a refrigerant having a temperature below the freezing point of water is provided in a space above the liquid mixture storage position of the heating means that heats the liquid mixture to a temperature higher than the evaporation temperature of water, and after the liquid mixture is heated by the heating means, It is characterized in that the refrigerant gas after the evaporated water in the mixed liquid is deposited as frost on the heat exchanger can be introduced into the low pressure section side of the refrigeration cycle through a pipe line provided above the heat exchanger. Separation and removal equipment for water, oil, etc. built into the refrigeration cycle.
JP1987111366U 1987-07-22 1987-07-22 Expired JPH0440136Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987111366U JPH0440136Y2 (en) 1987-07-22 1987-07-22

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987111366U JPH0440136Y2 (en) 1987-07-22 1987-07-22

Publications (2)

Publication Number Publication Date
JPS6416572U JPS6416572U (en) 1989-01-27
JPH0440136Y2 true JPH0440136Y2 (en) 1992-09-21

Family

ID=31349345

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987111366U Expired JPH0440136Y2 (en) 1987-07-22 1987-07-22

Country Status (1)

Country Link
JP (1) JPH0440136Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007051862A (en) * 2005-07-19 2007-03-01 Tokyo Electron Ltd Water removal device and inspection device in refrigerant

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5496448U (en) * 1977-12-20 1979-07-07

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007051862A (en) * 2005-07-19 2007-03-01 Tokyo Electron Ltd Water removal device and inspection device in refrigerant

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JPS6416572U (en) 1989-01-27

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