JPH06323697A - Oil separator for refrigerator - Google Patents

Oil separator for refrigerator

Info

Publication number
JPH06323697A
JPH06323697A JP5115590A JP11559093A JPH06323697A JP H06323697 A JPH06323697 A JP H06323697A JP 5115590 A JP5115590 A JP 5115590A JP 11559093 A JP11559093 A JP 11559093A JP H06323697 A JPH06323697 A JP H06323697A
Authority
JP
Japan
Prior art keywords
oil
pipe
flow
refrigerant gas
separation
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
JP5115590A
Other languages
Japanese (ja)
Inventor
Yoshio Haeda
芳夫 蝿田
Kensaku Kokuni
研作 小国
Hiroshi Yasuda
弘 安田
Susumu Nakayama
進 中山
Shinichiro Yamada
眞一朗 山田
Kenji Togusa
健治 戸草
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP5115590A priority Critical patent/JPH06323697A/en
Publication of JPH06323697A publication Critical patent/JPH06323697A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00Component parts or details not otherwise provided for in this subclass
    • F25B2400/02Centrifugal separation of gas, liquid or oil

Landscapes

  • Separating Particles In Gases By Inertia (AREA)

Abstract

(57)【要約】 【目的】冷凍機から吐出される冷媒ガスの中に含まれる
油を容易な分離機構そして小形で処理流量範囲の広い分
離性能を得ることの出来る油分離器を提供する。 【構成】油分離器は、冷拠配管内で分離する方法で、冷
媒ガスに旋回流を与える螺旋機構と管壁には油落し孔と
管の外側の2重管の油溜め部があり、底の油戻し管から
圧縮機に戻す機構から構成されている。最適な旋回流を
作ることにより高性能の分離機構が容易に達成できる。
(57) [Summary] [Object] To provide an oil separator that can easily separate oil contained in refrigerant gas discharged from a refrigerator and that is small in size and has a wide processing flow range separation performance. [Structure] An oil separator is a method of separating in a cold pipe, and has a spiral mechanism for giving a swirling flow to a refrigerant gas, an oil drop hole in a pipe wall, and an oil sump portion of a double pipe outside the pipe, It consists of a mechanism that returns the oil from the bottom oil return pipe to the compressor. A high-performance separation mechanism can be easily achieved by creating an optimum swirling flow.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は冷凍装置において、圧縮
機から吐出された高圧の冷媒ガス中に混入する冷凍機油
を分離するのに好適な機構を備えた冷凍装置の油分離器
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil separator for a refrigerating machine having a mechanism suitable for separating refrigerating machine oil mixed in high pressure refrigerant gas discharged from a compressor.

【0002】[0002]

【従来の技術】従来、この種の油分離器として、特開昭
60−106516号公報などのような構造が良く知られてお
り、図11に示したように、密閉容器51の上部に冷凍
ガス55aの入口管52,密閉容器51上部側面に出口管
53をそれぞれ接続され、密閉容器51の内部に油を分
離する円筒分離板54が垂直に取り付けられている。冷
媒ガス55aは入口管52から入り、円筒状分離板54
内側上部から下部側に流れ円筒状分離板54の矢印のよ
うに下側を通り上部の出口管53から冷媒ガスだけにな
り吐出ガス55bとして外へ吐出される。冷媒ガス55
aに含まれているミスト状の油は、円筒状分離板54内
側を通過する際に、自重の大きい油56は分離され下部
に溜る。密閉容器51の底には、油戻し管55がある。
2. Description of the Related Art Heretofore, as an oil separator of this type, Japanese Patent Laid-Open No.
A structure such as 60-106516 is well known, and as shown in FIG. 11, an inlet pipe 52 for the frozen gas 55a is provided on the upper portion of the closed container 51, and an outlet pipe 53 is provided on the upper side surface of the closed container 51. A cylindrical separation plate 54 that is connected and separates oil is vertically installed inside the closed container 51. Refrigerant gas 55a enters through the inlet pipe 52, and the cylindrical separation plate 54
It flows from the upper part to the lower part on the inner side, passes through the lower part as shown by the arrow of the cylindrical separating plate 54, and only the refrigerant gas is discharged from the upper outlet pipe 53 as discharge gas 55b to the outside. Refrigerant gas 55
When the mist-like oil contained in a passes through the inside of the cylindrical separation plate 54, the oil 56 having a large self-weight is separated and accumulated in the lower part. At the bottom of the closed container 51, there is an oil return pipe 55.

【0003】[0003]

【発明が解決しようとする課題】ところで図11に示す
油分離器の従来技術は、冷媒ガスの入口管52から密閉
容器51内に入り円筒状分離板54内に冷媒ガス55a
に含まれた油が、円筒状分離板54の下側を通過し上部
の出口管に向かって進む際に流れの方向が反転するため
に遠心力が働き冷媒ガスに比較して比重の大きな油は下
部に落して分離する機構である。しかし、処理流速が比
較的早くなると遠心による分離だけでは、効率が急速に
低下する。効率が上げるには、流速を小さくするため
に、大きな形状にしなければならない。この種の従来構
造の油分離器は、分離構造の寸法が大きくなり装置に取
り付ける場合に場所が必要となり装置全体的が大きくな
る。さらには、取り付け作業が困難になり、装置全体に
封入する油の量も多くなり、原価が高くなるなどの欠点
があった。分離器から出る油の量が多くなると熱交換器
の性能低下をはじめ膨張弁、及び、制御用弁の動作不良
の原因となる。
By the way, in the prior art of the oil separator shown in FIG. 11, a refrigerant gas 55a is introduced into a cylindrical separation plate 54 from a refrigerant gas inlet pipe 52 into a closed container 51.
When the oil contained in the oil passes through the lower side of the cylindrical separation plate 54 and advances toward the upper outlet pipe, the flow direction is reversed, so that centrifugal force acts and the oil having a larger specific gravity than the refrigerant gas. Is a mechanism that drops it down and separates it. However, when the processing flow rate is relatively high, the efficiency is rapidly decreased only by the separation by centrifugation. For higher efficiency, larger geometries must be used to reduce flow rates. In this type of conventional oil separator, the size of the separation structure becomes large, and a space is required when the oil separator is attached to the device, and the entire device becomes large. Further, there are drawbacks such that the mounting work becomes difficult, the amount of oil to be enclosed in the entire device increases, and the cost increases. If the amount of oil discharged from the separator increases, it may cause the performance of the heat exchanger to deteriorate and the malfunction of the expansion valve and the control valve.

【0004】本発明の目的は、冷媒配管内でしかも構造
が容易で分離効率の良い機構を提供することにある。
An object of the present invention is to provide a mechanism having a simple structure and a high separation efficiency in a refrigerant pipe.

【0005】[0005]

【課題を解決するための手段】本発明の分離機構は、冷
媒ガス管内のガスの流れを利用して油を分離するもので
あり、管内の流れを渦巻状にするので、冷媒ガスは旋回
しながら流れその時に発生する遠心力を利用して比重の
大きい油は配管の内壁に添って流れ、内壁には油の通る
孔を明け、この孔から油を落して分離する。ここでは、
管内のガスを旋回流にすることが重要で分離性能に影響
する。管内の冷媒ガスの流れを旋回流にするために、渦
巻状にした板を管内に挿入した構造、あるいは、スプリ
ングを挿入した構造などにより通路抵抗が小さくそして
構造が簡単で分離性能のよい機構により達成できる。
The separation mechanism of the present invention separates oil by utilizing the flow of gas in the refrigerant gas pipe. Since the flow in the pipe is made spiral, the refrigerant gas swirls. While flowing, the centrifugal force generated at that time causes the oil with a large specific gravity to flow along the inner wall of the pipe, and a hole through which the oil passes is opened in the inner wall, and the oil is dropped from this hole to separate it. here,
It is important to make the gas in the tube a swirl flow, which affects the separation performance. In order to make the flow of the refrigerant gas in the pipe a swirl flow, a structure in which a spiral plate is inserted in the pipe or a structure in which a spring is inserted has a small passage resistance and a mechanism with a simple structure and good separation performance. Can be achieved.

【0006】[0006]

【作用】冷凍装置の圧縮機から圧縮された高圧の冷媒ガ
スは、ねじり巻状の板を管内に挿入した油分機構部を通
過する際に旋回流が発生し、比重の大きい油には遠心力
が働くので管の内壁面に添って旋回しながら流れる。内
壁に多数の孔を明け流れる油を外側に設けた2重管の油
溜め部に溜める。溜った油は、戻し管により圧縮機側に
戻す。冷媒ガスの旋回流で流れる速さの変化は、渦巻状
の巻数を変化させることにより分離性能が向上出来る。
冷媒ガスの遠心作用の効果は、旋回流の流れによって決
まりそれに伴い、分離性能も決まる。
The high-pressure refrigerant gas compressed by the compressor of the refrigerating device generates a swirling flow when passing through the oil component mechanism part in which the spirally wound plate is inserted in the pipe, and centrifugal force is exerted on oil having a large specific gravity. Works, so it flows while swirling along the inner wall surface of the pipe. The oil flowing through many holes in the inner wall is stored in the oil reservoir of the double pipe provided outside. The accumulated oil is returned to the compressor side by the return pipe. The change of the flow speed of the swirling flow of the refrigerant gas can be improved by changing the number of spiral turns.
The effect of the centrifugal action of the refrigerant gas is determined by the flow of the swirling flow, and thus the separation performance is also determined.

【0007】[0007]

【実施例】以下、本発明の一実施例を図1により説明す
る。図2は図1の側面図を示し、図3は図1の分離機構
部の正面拡大図を示し、図4,図5,図6及び図7は応
用例を示し、図8,図9、および図10は、図7に示し
た分離部分の応用例を示したもので、図11は従来構造
を示す。図1は本発明の一実施例に係る油分機構の全体
側面図を示すものである。図中、1は冷媒ガス配管、2
は2重管になっている油溜め部、3は油戻し管、4はね
じり巻状の板、4aは破線で示した部分で、ねじり巻状
の板の裏側にあたる部分を示し、5は油抜き孔を示す。
次に、図1に示した油分離機構の動作について説明す
る。ここでは図示してないが、冷凍装置の圧縮機から吐
出された冷媒ガスaは、矢印aのように進みねじり巻状
の板4のところで、冷媒ガスaは配管1内壁を旋回流と
なり、その時に発生する遠心力が働き、比重の大きい油
は配管1内壁に添って旋回しながら流れ、配管1内壁に
明けた油抜き孔5から油溜め部2に落ちる。油溜め部2
に落ちた油は、油戻し管3から圧縮機へ戻す。ねじり巻
状の板2のねじり巻ピッチを変えることにより遠心力が
容易に変るので、したがって分離性能も変わる。ねじり
巻状の板4の長さを変化させても分離性能は変化する。
分離構造は簡単でしかも、管内部で分離出来ることから
場所もいらず安価である。図2は側面図を示したもの
で、油溜め部2は2重管になっており内側は冷媒配管1
で上部方向の位置にあり、油溜め部2に油6がたくさん
溜ってもよい構造にするためである。図3はねじり巻状
の板4部の拡大図を示したもので図から分かるように配
管1内壁とねじり巻状の板4の先端がお互いに接触して
いると冷媒ガスaの旋回が良くなり、したがって分離性
能も向上する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. 2 shows a side view of FIG. 1, FIG. 3 shows an enlarged front view of the separation mechanism portion of FIG. 1, FIGS. 4, 5, 6 and 7 show application examples, and FIGS. 10 and 10 show an application example of the separation part shown in FIG. 7, and FIG. 11 shows a conventional structure. FIG. 1 shows an overall side view of an oil content mechanism according to an embodiment of the present invention. In the figure, 1 is a refrigerant gas pipe, 2
Is an oil sump which is a double pipe, 3 is an oil return pipe, 4 is a twist-wound plate, 4a is a part shown by a broken line, and a part corresponding to the back side of the twist-wound plate is shown, and 5 is an oil Indicates a punched hole.
Next, the operation of the oil separation mechanism shown in FIG. 1 will be described. Although not shown here, the refrigerant gas a discharged from the compressor of the refrigerating apparatus advances as shown by the arrow a, and at the twist-wound plate 4, the refrigerant gas a becomes a swirling flow on the inner wall of the pipe 1 at that time. Due to the centrifugal force generated in the oil, the oil having a large specific gravity flows while swirling along the inner wall of the pipe 1 and falls into the oil sump 2 from the oil drain hole 5 opened in the inner wall of the pipe 1. Oil sump part 2
The oil that has dropped to the compressor is returned from the oil return pipe 3 to the compressor. The centrifugal force is easily changed by changing the twist winding pitch of the twist wound plate 2, and therefore the separation performance is also changed. The separation performance changes even if the length of the twist-wound plate 4 is changed.
The separation structure is simple, and since it can be separated inside the pipe, it does not take up space and is inexpensive. FIG. 2 is a side view showing that the oil sump portion 2 is a double pipe and the inside is the refrigerant pipe 1
This is for the purpose of providing a structure in which a large amount of oil 6 can be accumulated in the oil sump portion 2 because it is located at the upper position. FIG. 3 is an enlarged view of the twist-wound plate 4, and as can be seen from the figure, when the inner wall of the pipe 1 and the tip of the twist-wound plate 4 are in contact with each other, the swirling of the refrigerant gas a is good. Therefore, the separation performance is also improved.

【0008】次に、油分離機構の応用例を図4を用いて
説明する。冷媒ガスaに旋回流を与える方法として管内
にスプリング4bを挿入したものであり、冷媒配管1が
曲がっている所でも使用可能であり、また、スプリング
4bのピッチを変えることにより分離性能を変えること
ができる。この分離機構は、構造が容易であるため安価
である。
Next, an application example of the oil separation mechanism will be described with reference to FIG. As a method of giving a swirling flow to the refrigerant gas a, a spring 4b is inserted in the pipe, and it can be used even in a place where the refrigerant pipe 1 is bent, and the separation performance can be changed by changing the pitch of the spring 4b. You can This separation mechanism is inexpensive because of its simple structure.

【0009】次に、油分離機構の応用例を図5を用いて
説明する。この方法は、冷媒配管1の間にファン7を取
り付け、冷媒ガスaの流力によりファン7が回転してフ
ァン7の羽根に当たって油を吹き飛ばして分離する機構
である。8はシャフト、9は冷媒ガス通路、10は軸受
部を示す。冷媒ガスaの流れが速いとファン7の回転が
早くなるので沢山の油を吹き飛ばすことが出来ることか
ら分離性能が良くなる。ファン7の羽根の形状や傾きそ
して枚数などを変えることによっても分離性能を向上さ
せることが出来る利点がある。さらには、ファン7の羽
根の寸法を変えることによっても、分離性能を向上させ
ることが出来る等の利点がある。
Next, an application example of the oil separation mechanism will be described with reference to FIG. This method is a mechanism in which a fan 7 is mounted between the refrigerant pipes 1 and the fan 7 is rotated by the flow force of the refrigerant gas a and hits the blades of the fan 7 to blow off the oil and separate the oil. 8 is a shaft, 9 is a refrigerant gas passage, and 10 is a bearing. When the flow of the refrigerant gas a is fast, the rotation of the fan 7 is fast, and a large amount of oil can be blown off, so that the separation performance is improved. There is an advantage that the separation performance can be improved also by changing the shape, inclination, and number of blades of the fan 7. Further, there is an advantage that the separation performance can be improved by changing the size of the blade of the fan 7.

【0010】次に、油分機構の応用例を図6を用いて説
明する。図1に示した実施例と基本的には同じ分離機構
であるが、管内の冷媒ガスaの流れを旋回させる機構と
して、螺旋形状4cにしたものである。螺旋形状4c
は、容易に作ることが出来る。さらには、螺旋形状4c
のピッチを変えることにより冷媒ガスaの旋回速度が変
わるので、したがって遠心力も変わり油の分離性能が容
易に向上出来る。
Next, an application example of the oil content mechanism will be described with reference to FIG. Although the separation mechanism is basically the same as that of the embodiment shown in FIG. 1, it has a spiral shape 4c as a mechanism for swirling the flow of the refrigerant gas a in the pipe. Spiral shape 4c
Can be made easily. Furthermore, spiral shape 4c
Since the swirling speed of the refrigerant gas a changes by changing the pitch of, the centrifugal force also changes and the oil separation performance can be easily improved.

【0011】次に、油分離機構の応用例を図7を用いて
説明する。ここで示した分離機構は、冷媒ガスaの流れ
に旋回流を与えるのではなく、流れに対してボリューム
の変化を利用して分離するもので、邪魔板4dを挿入し
冷媒ガスを流すことにより、圧縮,膨張,拡散作用を繰
り返すことにより分離する機構である。さらには、圧
縮,膨張,拡散作用の繰り返し構造の応用例を図8,図
9および図10に示す。図8に示した邪魔板4eは、冷
媒配管の内壁と邪魔板4eとの隙間を冷媒ガスがスムー
ズに流れるように先端部pにR形状を付けた構造であ
る。これは、通路抵抗を小さくするためである。次に、
図9に示した邪魔板4fは、流れに対して各々のボリュ
ームに変化を持たせた構造で、同じ分離機構の寸法に対
しては、比較的分離性能を向上出来る機構である。次
に、図10に示した邪魔板4jは、冷媒配管と邪魔板4
jとの隙間を各ボリューム毎に圧縮,膨張,拡散作用の
繰り返しに変化をもたせた邪魔板4j構造である。冷媒
ガスaの流れを乱すことにより分離性能の向上を図った
ものである。分離性能の値に対して、圧力損失が小さい
利点がある。
Next, an application example of the oil separation mechanism will be described with reference to FIG. The separation mechanism shown here does not give a swirl flow to the flow of the refrigerant gas a, but separates it by utilizing the change in volume with respect to the flow. By inserting the baffle plate 4d and flowing the refrigerant gas. It is a mechanism that separates by repeating compression, expansion, and diffusion. Further, application examples of the repeating structure of compression, expansion and diffusion action are shown in FIGS. 8, 9 and 10. The baffle plate 4e shown in FIG. 8 has a structure in which the tip portion p has an R shape so that the refrigerant gas can smoothly flow through the gap between the inner wall of the refrigerant pipe and the baffle plate 4e. This is to reduce the passage resistance. next,
The baffle plate 4f shown in FIG. 9 has a structure in which each volume is changed with respect to the flow, and is a mechanism that can relatively improve the separation performance for the same size of the separation mechanism. Next, the baffle plate 4j shown in FIG.
The baffle plate 4j has a structure in which a gap with j is changed in repetition of compression, expansion and diffusion for each volume. The separation performance is improved by disturbing the flow of the refrigerant gas a. There is an advantage that the pressure loss is small with respect to the value of the separation performance.

【0012】これまで述べてきた図1から応用例の図7
までの分離機構は、水平方向の冷媒ガスの流れについて
述べてきたが、冷媒配管の垂直方向の流れに対しても使
用は可能であり、さらには、配管の曲がっているところ
も良い。従来の油分離機構と全く異なる分離機構であ
り、特に、冷媒ガスの配管内で油を分離する機構から、
寸法からくる制約、あるいは、冷凍装置の使用条件から
くる制約などもないため、高性能な分離機構が達成でき
る。
From FIG. 1 described so far to FIG. 7 of an application example.
The separating mechanism up to has been described with respect to the flow of the refrigerant gas in the horizontal direction, but it can be used for the flow in the vertical direction of the refrigerant pipe, and the pipe may be bent. It is a completely different separation mechanism from the conventional oil separation mechanism, especially from the mechanism for separating oil in the refrigerant gas pipe,
Since there are no restrictions due to the size or the usage conditions of the refrigeration system, a high-performance separation mechanism can be achieved.

【0013】[0013]

【発明の効果】本発明によれば、これまで欠点となって
いた油分離器の構造が大きいために、使い勝手が悪い、
あるいは、冷媒ガスの流れ分離性能のなかで、圧縮機の
容量制御により回転数が変化するので、冷媒ガスの吐出
量が変り油分離器の処理流速も同様に変化してくる。油
分離器は処理流速に分離性能が影響し、早くなると大幅
に分離性能は低下し、冷凍装置でも油により性能が低下
していた。今回、開発した分離機構は、冷媒配管内で油
を分離させること、処理流速の変化に対して分離性能は
影響されない利点がある。さらには、分離機構は冷媒配
管の形状と同等であること、容易な構造であること、し
たがって小形であるので安価で出来る。
According to the present invention, since the structure of the oil separator, which has been a drawback so far, is large, the usability is poor.
Alternatively, in the flow separation performance of the refrigerant gas, the rotational speed changes due to the capacity control of the compressor, so the discharge amount of the refrigerant gas changes and the processing flow velocity of the oil separator also changes. The separation performance of the oil separator has an effect on the processing flow rate, and the separation performance is significantly deteriorated as the processing speed increases, and the performance of the refrigeration system is also deteriorated by oil. The separation mechanism developed this time has the advantage of separating oil in the refrigerant pipe and that the separation performance is not affected by changes in the processing flow rate. Furthermore, since the separating mechanism has the same shape as that of the refrigerant pipe, has an easy structure, and is small in size, it can be manufactured at low cost.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例に係る油分離器の全体構造の
断面図。
FIG. 1 is a sectional view of the overall structure of an oil separator according to an embodiment of the present invention.

【図2】図1の側面図。FIG. 2 is a side view of FIG.

【図3】図1に示す分離機構の拡大図。FIG. 3 is an enlarged view of the separation mechanism shown in FIG.

【図4】応用例の断面図。FIG. 4 is a cross-sectional view of an application example.

【図5】応用例の断面図。FIG. 5 is a cross-sectional view of an application example.

【図6】応用例の断面図。FIG. 6 is a cross-sectional view of an application example.

【図7】応用例の断面図。FIG. 7 is a cross-sectional view of an application example.

【図8】図7に示した分離機構である邪魔板の応用例の
断面図。
8 is a cross-sectional view of an application example of a baffle plate that is the separation mechanism shown in FIG.

【図9】図7に示した分離機構である邪魔板の応用例の
断面図。
9 is a cross-sectional view of an application example of a baffle plate that is the separation mechanism shown in FIG.

【図10】図7に示した分離機構である邪魔板の応用例
の断面図。
10 is a cross-sectional view of an application example of the baffle plate that is the separation mechanism shown in FIG.

【図11】従来の全体構造図の断面図。FIG. 11 is a sectional view of a conventional overall structural view.

【符号の説明】[Explanation of symbols]

1…冷媒ガス管、2…油溜め部、3…油戻し管、4…ね
じり巻状の板、4a…ねじり巻の板の裏側になる部分、
4b…スプリング形状、4c…螺旋形状、4d,4e,
4f,4j…邪魔板、5…油抜き孔、p…先端部。
DESCRIPTION OF SYMBOLS 1 ... Refrigerant gas pipe, 2 ... Oil sump part, 3 ... Oil return pipe, 4 ... Twist-wound plate, 4a ...
4b ... spring shape, 4c ... spiral shape, 4d, 4e,
4f, 4j ... baffle plate, 5 ... oil drain hole, p ... tip portion.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中山 進 茨城県土浦市神立町502番地 株式会社日 立製作所機械研究所内 (72)発明者 山田 眞一朗 静岡県清水市村松390番地 株式会社日立 製作所清水工場内 (72)発明者 戸草 健治 静岡県清水市村松390番地 株式会社日立 製作所清水工場内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Susumu Nakayama 502 Jinritsucho, Tsuchiura-shi, Ibaraki Machinery Research Institute, Hiritsu Manufacturing Co., Ltd. Inside the factory (72) Inventor Kenji Togusa 390 Muramatsu, Shimizu City, Shizuoka Prefecture Hitachi Ltd. Shimizu factory

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】冷凍装置の圧縮機から吐出される高圧の冷
媒ガス内に含まれるミスト状の油を分離する油分離器に
おいて、管内の流れを渦巻流にして遠心力による油分離
し、分離された油は内壁の孔から外側に設けた2重管の
油溜めに落ち、分離された油を戻す機構を備えているこ
とを特徴とする冷凍装置の油分離器。
1. An oil separator for separating mist-like oil contained in a high-pressure refrigerant gas discharged from a compressor of a refrigerating apparatus, in which a flow in a tube is made into a spiral flow to separate oil by centrifugal force and to separate the oil. An oil separator of a refrigerating device, characterized in that the oil thus collected falls from a hole in the inner wall into an oil reservoir of a double pipe provided outside and returns the separated oil.
【請求項2】請求項1において、管内の流れを渦巻流に
させる機構は、一枚の板を螺旋状とし、直径は管内径と
ほぼ同じ寸法で、巻数は配管の長手方向として、遠心力
による分離機構を備えている冷凍装置の油分離器。
2. The mechanism according to claim 1, wherein the mechanism for making the flow in the pipe into a spiral flow is such that one plate has a spiral shape, the diameter is approximately the same as the pipe inner diameter, and the number of turns is the longitudinal direction of the pipe, and centrifugal force is applied. Oil separator of refrigeration equipment equipped with a separation mechanism by.
【請求項3】請求項1において、管内の流れを渦巻流に
させる機構は、管内径とほぼ同じ寸法形状にしたスプリ
ングを挿入し遠心作用による分離機構を備えている冷凍
装置の油分離器。
3. The oil separator of a refrigerating apparatus according to claim 1, wherein the mechanism for making the flow in the pipe a spiral flow has a separation mechanism by centrifugal action in which a spring having a size and shape similar to the pipe inner diameter is inserted.
【請求項4】請求項1において、管内にファンを取り付
け、冷媒ガスの流力によりファンは回転し、ファンの回
転力により羽根の回転による慣性力で油を吹き飛ばして
分離する機構を備えている冷凍装置の油分離器。
4. A mechanism according to claim 1, wherein a fan is installed in the pipe, the fan is rotated by the flow force of the refrigerant gas, and the rotating force of the fan blows off and separates the oil by the inertial force generated by the rotation of the blades. Oil separator for refrigeration equipment.
JP5115590A 1993-05-18 1993-05-18 Oil separator for refrigerator Pending JPH06323697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5115590A JPH06323697A (en) 1993-05-18 1993-05-18 Oil separator for refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5115590A JPH06323697A (en) 1993-05-18 1993-05-18 Oil separator for refrigerator

Publications (1)

Publication Number Publication Date
JPH06323697A true JPH06323697A (en) 1994-11-25

Family

ID=14666375

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5115590A Pending JPH06323697A (en) 1993-05-18 1993-05-18 Oil separator for refrigerator

Country Status (1)

Country Link
JP (1) JPH06323697A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006258413A (en) * 2005-02-18 2006-09-28 Fuji Electric Retail Systems Co Ltd Mixed fluid separation apparatus
KR101024475B1 (en) * 2004-02-11 2011-03-23 엘지전자 주식회사 Compressor Oil Supply Structure of Air Conditioner
JP2013167384A (en) * 2012-02-15 2013-08-29 Hitachi Appliances Inc Air conditioner
WO2014083674A1 (en) * 2012-11-30 2014-06-05 三菱電機株式会社 Compressor, refrigeration cycle device, and heat pump hot-water supply device
JPWO2014083901A1 (en) * 2012-11-30 2017-01-05 三菱電機株式会社 Refrigeration cycle apparatus and heat pump water heater
WO2019229814A1 (en) * 2018-05-28 2019-12-05 三菱電機株式会社 Oil separator and refrigeration cycle device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101024475B1 (en) * 2004-02-11 2011-03-23 엘지전자 주식회사 Compressor Oil Supply Structure of Air Conditioner
JP2006258413A (en) * 2005-02-18 2006-09-28 Fuji Electric Retail Systems Co Ltd Mixed fluid separation apparatus
JP2013167384A (en) * 2012-02-15 2013-08-29 Hitachi Appliances Inc Air conditioner
WO2014083674A1 (en) * 2012-11-30 2014-06-05 三菱電機株式会社 Compressor, refrigeration cycle device, and heat pump hot-water supply device
WO2014083901A1 (en) * 2012-11-30 2014-06-05 三菱電機株式会社 Compressor, refrigeration cycle device, and heat pump hot-water supply device
JPWO2014083901A1 (en) * 2012-11-30 2017-01-05 三菱電機株式会社 Refrigeration cycle apparatus and heat pump water heater
WO2019229814A1 (en) * 2018-05-28 2019-12-05 三菱電機株式会社 Oil separator and refrigeration cycle device
JPWO2019229814A1 (en) * 2018-05-28 2020-12-10 三菱電機株式会社 Oil separator and refrigeration cycle equipment

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