JPH1019423A - Oil separator - Google Patents

Oil separator

Info

Publication number
JPH1019423A
JPH1019423A JP17607396A JP17607396A JPH1019423A JP H1019423 A JPH1019423 A JP H1019423A JP 17607396 A JP17607396 A JP 17607396A JP 17607396 A JP17607396 A JP 17607396A JP H1019423 A JPH1019423 A JP H1019423A
Authority
JP
Japan
Prior art keywords
oil
container body
refrigerant
opening
partition plate
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
JP17607396A
Other languages
Japanese (ja)
Inventor
Takashi Kaneko
孝 金子
Masao Kurachi
正夫 蔵地
Kazuhiko Marumoto
一彦 丸本
Michiyoshi Kusaka
道美 日下
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 Matsushita Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP17607396A priority Critical patent/JPH1019423A/en
Publication of JPH1019423A publication Critical patent/JPH1019423A/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

PROBLEM TO BE SOLVED: To prevent a decrease in an oil separating capacity of a centrifugal separation by holding an inner diameter of a centrifugal separator small even if an inner diameter of a container body is increased to increase a sectional area of a separating material for the purpose of increasing a capacity of an oil reservoir or improving oil separating performance. SOLUTION: The oil separator comprises a structure that an upper part of a container body 10 is separated into an inside chamber 12 and an outside chamber 13 by a cylindrical partition plate 11 of a predetermined length opened at a lower part provided at a vertical lower part from an inner upper end of the body 10 and a refrigerant inlet 15 having an opening at an upper part in the chamber 12 is provided in a tangential direction at the plate 11, a refrigerant outlet 16 having an opening at an upper part in the chamber 13 is provided at the outside of the body 10, and a separating material 18 inclined down toward the inside surface of the body 10 is provided horizontally at the entire surface of the chamber 13 near a lower part of the outlet 16.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、冷凍サイクルにお
いて、圧縮機から吐出された気相冷媒中に含まれる油を
分離する油分離器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil separator for separating oil contained in a gas-phase refrigerant discharged from a compressor in a refrigeration cycle.

【0002】[0002]

【従来の技術】従来、この種の油分離器として、例え
ば、実開平5−141815号公報に示されている様な
油分離器である。
2. Description of the Related Art Conventionally, as an oil separator of this type, for example, an oil separator as disclosed in Japanese Utility Model Laid-Open No. 5-141815 is known.

【0003】以下、図面を参照しながら上述した油分離
器について説明する。尚、図中の実践の矢印は冷媒の流
れを、点線の矢印は油の流れを示す。
Hereinafter, the oil separator described above will be described with reference to the drawings. Note that the practice arrows in the figure indicate the flow of the refrigerant, and the dotted arrows indicate the flow of the oil.

【0004】図9において、容器本体1の内部は、水平
方向に設けた所定の大きさの開口部2aを有する円盤形
状の仕切板2により、下側室3と上側室4に分離され
る。また、下側室3の下部は油溜まり部5とする。ま
た、6は冷媒入口管であり、容器本体1の外側の接線方
向から下側室3内に連通し、下側室3内の上部に開口部
を有する。7は冷媒出口管であり、容器本体1の外側か
ら上側室4に連通し、上側室4内の上部に開口部を有す
る。8は油排出管であり、容器本体1の外側から油溜ま
り部5に連通し、油溜まり部5の底部近傍に開口部を有
する。9は分離材であり、冷媒出口管7の開口部の下方
近傍の水平方向に上側室4全面に設けられている。
In FIG. 9, the inside of a container body 1 is separated into a lower chamber 3 and an upper chamber 4 by a disk-shaped partition plate 2 having a predetermined size opening 2a provided in a horizontal direction. The lower portion of the lower chamber 3 is an oil reservoir 5. Reference numeral 6 denotes a refrigerant inlet pipe, which communicates with the inside of the lower chamber 3 from a tangential direction outside the container body 1 and has an opening in the upper part of the lower chamber 3. Reference numeral 7 denotes a refrigerant outlet pipe, which communicates with the upper chamber 4 from the outside of the container body 1 and has an opening in the upper part of the upper chamber 4. Reference numeral 8 denotes an oil discharge pipe, which communicates with the oil reservoir 5 from outside the container body 1 and has an opening near the bottom of the oil reservoir 5. Reference numeral 9 denotes a separating member, which is provided on the entire upper chamber 4 in the horizontal direction near the bottom of the opening of the refrigerant outlet pipe 7.

【0005】次に、上記構成の油分離器内の冷媒及び油
の拳動について説明する。まず、圧縮機から吐出された
油を含む気相冷媒は、冷媒入口管6から下側室3の上部
に導かれ、旋回下降流を生成し遠心力によって油が分離
される。この分離された油は重力により容器本体1の内
側面に伝い下降し、油溜まり部5に落下する。その後、
冷媒は仕切板2の開口部2aを通して上側室4の下部に
導かれ、分離材9を通過し、上側室4の上部に導かれ
る。この時、分離材9では冷媒中に含まれる油を捕集す
るため、さらに油が分離される。この分離された油は、
重力により、油溜まり部5に落下する。その後、冷媒は
冷媒出口管7よりサイクルに戻される。また、油溜まり
部5に落下した油は、油排出口8より圧縮機に吸入側に
もどされる。
Next, the fisting of the refrigerant and oil in the oil separator having the above configuration will be described. First, the gaseous refrigerant containing oil discharged from the compressor is guided from the refrigerant inlet pipe 6 to the upper part of the lower chamber 3, generates a swirling downward flow, and the oil is separated by centrifugal force. The separated oil travels down the inner surface of the container body 1 due to gravity and falls into the oil reservoir 5. afterwards,
The refrigerant is guided to the lower part of the upper chamber 4 through the opening 2 a of the partition plate 2, passes through the separating member 9, and is guided to the upper part of the upper chamber 4. At this time, the separating material 9 collects oil contained in the refrigerant, so that the oil is further separated. This separated oil,
Due to gravity, it falls into the oil reservoir 5. Thereafter, the refrigerant is returned to the cycle through the refrigerant outlet pipe 7. The oil that has fallen into the oil reservoir 5 is returned to the compressor from the oil discharge port 8 to the suction side.

【0006】[0006]

【発明が解決しようとする課題】しかしながら上記のよ
うな構成では、オイル溜まり部5の容量の増加、或い
は、油分離性能の向上を目的とした分離材9の断面積の
増加のために容器本体1の内径を大きくすると、遠心分
離を行う下側室3の内径が大きくなってしまう。そのた
め、冷媒の旋回半径に反比例する遠心力が低下し、遠心
分離による油分離能力の定価の問題があった。
However, in the above configuration, the container body is increased in order to increase the capacity of the oil reservoir 5 or to increase the sectional area of the separating material 9 for the purpose of improving the oil separation performance. If the inside diameter of 1 is increased, the inside diameter of the lower chamber 3 for performing centrifugation becomes large. For this reason, the centrifugal force, which is inversely proportional to the turning radius of the refrigerant, decreases, and there is a problem in the price of the oil separation ability by centrifugation.

【0007】本発明は従来の課題を解決するもので、オ
イル溜まり部の容量の増加、或いは、油分離性能の向上
を目的とした分離材の断面積の増加のために容器本体の
内径を大きくした場合でも、遠心分離部での油分離能力
の低下の防止が可能な油分離器を提供することを目的と
する。
SUMMARY OF THE INVENTION The present invention solves the conventional problems, in which the inner diameter of a container body is increased to increase the capacity of an oil reservoir or the cross-sectional area of a separating material for the purpose of improving oil separation performance. It is an object of the present invention to provide an oil separator capable of preventing a decrease in oil separation capacity in a centrifugal separation section even in the case where the oil separator is used.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に本発明は、容器本体の内部上端より下方垂直に設けた
下方が開口した所定長さの円筒形状の仕切板と、前記仕
切板により容器本体内の上部を内側室と外側室に分離
し、前記仕切板より下方を油溜まり部とするとともに、
容器本体の外側から前記仕切板の接線方向に前記内側室
に連通し、前記内側室内の上部に開口部を有する冷媒入
口管と、容器本体の外側からに前記外側室に連通し、前
記外側室内の上部に開口部を有する冷媒出口管と、容器
本体の外側から前記油溜まり部に連通し、前記油溜まり
部の底部近傍に開口部を有する油排出管と、前記冷媒出
口管の開口部の下方近傍の水平方向に前記外側室全面に
容器本体の内側面に向かって下方に傾斜している分離材
を設けた構造としている。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention is directed to a cylindrical partition plate having a predetermined length, which is provided vertically below the upper end of the inside of a container body and has a downwardly opened lower part, and the partition plate. The upper part in the container body is separated into an inner chamber and an outer chamber, and the lower part than the partition plate as an oil reservoir,
A refrigerant inlet pipe communicating from the outside of the container body to the inner chamber in a tangential direction of the partition plate and having an opening at an upper portion of the inner chamber; and a refrigerant inlet pipe communicating from the outside of the container body to the outer chamber; A refrigerant outlet pipe having an opening at an upper portion thereof, an oil discharge pipe communicating from the outside of the container body to the oil reservoir, and having an opening near a bottom of the oil reservoir, and an opening of the refrigerant outlet pipe. In the horizontal direction near the lower part, a separating member inclined downward toward the inner surface of the container body is provided on the entire surface of the outer chamber.

【0009】また、容器本体の内部上端より下方垂直に
設けた下方が開口した所定長さの円筒形状の仕切板と、
前記仕切板により容器本体内の上部を内側室と外側室に
分離し、前記仕切板より下方を油溜まり部とするととも
に、容器本体の上面から前記内側室に連通し、前記内側
室内の上部に前記仕切板の接線方向に冷媒を吐き出す開
口部を有する冷媒入口管と、容器本体の外側から前記外
側室に連通し、前記外側室内の上部に開口部を有する冷
媒出口管と、容器本体の外側から前記油溜まり部に連通
し、前記油溜まり部の底部近傍に開口部を有する油排出
管と、前記冷媒出口管の開口部の下方近傍の水平方向に
前記外側室全面に容器本体の内側面に向かって下方に傾
斜している分離材を設けた構造としている。
A cylindrical partition plate having a predetermined length and having a downward opening and provided vertically below the upper end of the inside of the container body;
The upper part in the container body is separated into an inner chamber and an outer chamber by the partition plate, and the lower part than the partition plate is an oil reservoir, and the upper part of the container body communicates with the inner chamber from the upper surface of the container body. A refrigerant inlet pipe having an opening for discharging refrigerant in a tangential direction of the partition plate, a refrigerant outlet pipe communicating from the outside of the container body to the outer chamber, and having an opening in an upper part of the outer chamber; An oil discharge pipe communicating with the oil sump from above and having an opening near the bottom of the oil sump; and an inner surface of the container body on the entire surface of the outer chamber in a horizontal direction near a position below the opening of the refrigerant outlet pipe. It has a structure in which a separating material inclined downward toward is provided.

【0010】また、容器本体の内部上端より下方垂直に
設けた下方に向かって径が小となり下方が開口した所定
長さの円錐形状の仕切板と、前記仕切板により容器本体
内の上部を内側室と外側室に分離し、前記仕切板より下
方を油溜まり部とするとともに、容器本体の外側から前
記仕切板の接線方向に前記内側室に連通し、前記内側室
内の上部に開口部を有する冷媒入口管と、容器本体の外
側からに前記外側室に連通し、前記外側室内の上部に開
口部を有する冷媒出口管と、容器本体の外側から前記油
溜まり部に連通し、前記油溜まり部の底部近傍に開口部
を有する油排出管と、前記冷媒出口管の開口部の下方近
傍の水平方向に前記外側室全面に容器本体の内側面に向
かって下方に傾斜している分離材を設けた構造としてい
る。
[0010] Further, a conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a downwardly decreasing diameter and is opened downward, has an upper part inside the container body inside by the partition plate. The partition is separated into a chamber and an outer chamber, and a portion below the partition plate is used as an oil sump portion, and communicates from the outside of the container body to the inner chamber in a tangential direction of the partition plate, and has an opening at an upper portion of the inner chamber. A refrigerant inlet pipe, a refrigerant outlet pipe communicating with the outer chamber from outside the container body, and having an opening in an upper part of the outer chamber; and a refrigerant sump part communicating with the oil reservoir from outside the container main body. An oil discharge pipe having an opening in the vicinity of the bottom of the container, and a separating member inclined downward toward the inner surface of the container body over the entire outer chamber in a horizontal direction near the opening of the refrigerant outlet pipe. Structure.

【0011】また、容器本体の内部上端より下方垂直に
設けた下方に向かって径が小となり下方が開口した所定
長さの円錐形状の仕切板と、前記仕切板により容器本体
内の上部を内側室と外側室に分離し、前記仕切板より下
方を油溜まり部とするとともに、容器本体の上面から前
記内側室に連通し、前記内側室内の上部に前記仕切板の
接線方向に冷媒を吐き出す開口部を有する冷媒入口管
と、容器本体の外側から前記外側室に連通し、前記外側
室内の上部に開口部を有する冷媒出口管と、容器本体の
外側から前記油溜まり部に連通し、前記油溜まり部の底
部近傍に開口部を有する油排出管と、前記冷媒出口管の
開口部の下方近傍の水平方向に前記外側室全面に容器本
体の内側面に向かって下方に傾斜している分離材を設け
た構造としている。
[0011] Further, a conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a downwardly decreasing diameter and is open downward, has an upper part inside the container body inside by the partition plate. An opening which is separated into a chamber and an outer chamber, and has an oil reservoir below the partition plate, communicates with the inner chamber from the upper surface of the container body, and discharges refrigerant in an upper part of the inner chamber in a tangential direction of the partition plate. A refrigerant inlet pipe having a portion, a refrigerant outlet pipe communicating from the outside of the container body to the outer chamber, and a refrigerant outlet pipe having an opening in an upper portion of the outer chamber; An oil discharge pipe having an opening near the bottom of the reservoir, and a separating member inclined downwardly toward the inner surface of the container body over the entire outer chamber in the horizontal direction near the bottom of the opening of the refrigerant outlet pipe. Is provided.

【0012】これにより、遠心分離部での油分離能力の
低下を防止できる。
[0012] Thus, it is possible to prevent the oil separating ability from being reduced in the centrifugal separator.

【0013】[0013]

【発明の実施の形態】請求項1に記載の発明は、容器本
体の内部上端より下方垂直に設けた下方が開口した所定
長さの円筒形状の仕切板により、容器本体内の上部を内
側室と外側室に分離し、前記仕切板より下方を油溜まり
部とする。さらに、容器本体の外側から前記仕切板の接
線方向に前記内側室に連通し、前記内側室内の上部に開
口部を有する冷媒入口管と、容器本体の外側からに前記
外側室に連通し、前記外側室内の上部に開口部を有する
冷媒出口管と、容器本体の外側から前記油溜まり部に連
通し、前記油溜まり部の底部近傍に開口部を有する油排
出管と、前記冷媒出口管の開口部の下方近傍の水平方向
に前記外側室全面に容器本体の内側面に向かって下方に
傾斜している分離材を設ける構造としたことにより、オ
イル溜まり部の容量の増加、或いは、油分離性能の向上
を目的とした分離材の断面積の増加のために容器本体の
内径を大きくしても、遠心分離を行う内側室の内径が大
きくならない。従って、冷媒の旋回半径に反比例する遠
心力の低下による、油分離能力の低下を防止できる。ま
た、分離材を容器本体の内側面に向けて下方に傾斜させ
ているため、分離材に付着したオイルが容器本体の内側
面へ流動し、分離材へのオイルの付着による油分離能力
の低下を防止でき、そして、オイルは容器本体の内側面
を伝い油溜まり部に落下するため、内側室から外側室に
向かう冷媒によるオイルの再飛散による油分離能力の低
下を防止でき、さらに、分離材の断面積が増加するため
分離材通過時の冷媒の流速が低下し、油分離能力を向上
できる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention according to the first aspect of the present invention is directed to an invention in which an upper portion in a container body is formed in an inner chamber by a cylindrical partition plate having a predetermined length opened vertically downward from an upper end inside the container body. And an outer chamber, and a portion below the partition plate is an oil reservoir. Further, the refrigerant chamber communicates with the inner chamber in a tangential direction of the partition plate from outside the container body, and a refrigerant inlet pipe having an opening at an upper portion of the inner chamber, and communicates with the outer chamber from outside the container body, A refrigerant outlet pipe having an opening in the upper part of the outer chamber, an oil discharge pipe communicating with the oil reservoir from outside the container body, and having an opening near the bottom of the oil reservoir, and an opening of the refrigerant outlet pipe In the horizontal direction near the lower part of the container, a separating member inclined downward toward the inner surface of the container body is provided on the entire surface of the outer chamber, so that the capacity of the oil reservoir portion is increased or the oil separating performance is increased. Even if the inner diameter of the container body is increased in order to increase the cross-sectional area of the separation material for the purpose of improving the inner diameter, the inner diameter of the inner chamber for centrifugal separation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.

【0014】また、請求項2に記載の発明は、容器本体
の内部上端より下方垂直に設けた下方が開口した所定長
さの円筒形状の仕切板により容器本体内の上部を内側室
と外側室に分離し、前記仕切板より下方を油溜まり部と
する。さらに、容器本体の上面から前記内側室に連通
し、前記内側室内の上部に前記仕切板の接線方向に冷媒
を吐き出す開口部を有する冷媒入口管と、容器本体の外
側から前記外側室に連通し、前記外側室内の上部に開口
部を有する冷媒出口管と、容器本体の外側から前記油溜
まり部に連通し、前記油溜まり部の底部近傍に開口部を
有する油排出管と、前記冷媒出口管の開口部の下方近傍
の水平方向に前記外側室全面に容器本体の内側面に向か
って下方に傾斜している分離材を設ける構造としたこと
により、オイル溜まり部の容量の増加、或いは、油分離
性能の向上を目的とした分離材の断面積の増加のために
容器本体の内径を大きくしても、遠心分離を行う内側室
の内径が大きくならない。従って、冷媒の旋回半径に反
比例する遠心力の低下による、油分離能力の低下を防止
できる。また、分離材を容器本体の内側面に向けて下方
に傾斜させているため、分離材に付着したオイルが容器
本体の内側面へ流動し、分離材へのオイルの付着による
油分離能力の低下を防止でき、そして、オイルは容器本
体の内側面を伝い油溜まり部に落下するため、内側室か
ら外側室に向かう冷媒によるオイルの再飛散による油分
離能力の低下を防止でき、さらに、分離材の断面積が増
加するため分離材通過時の冷媒の流速が低下し、油分離
能力を向上できる。また、冷媒入口管を容器本体の上面
から内側室に連通させたため、冷媒入口管設置のための
穴あけ作業及び溶接作業が1箇所のみであり、製造工数
も低減できる。
According to a second aspect of the present invention, the upper portion of the inside of the container body has an inner chamber and an outer chamber which are provided vertically below the upper end of the container body and are provided with a cylindrical partition plate having a predetermined length and opened downward. And the portion below the partition plate is defined as an oil reservoir. Further, a refrigerant inlet pipe communicating with the inner chamber from the upper surface of the container body and having an opening at the upper part of the inner chamber for discharging refrigerant in a tangential direction of the partition plate, and communicating with the outer chamber from outside the container body. A refrigerant outlet pipe having an opening at an upper part in the outer chamber, an oil discharge pipe communicating with the oil reservoir from outside the container body, and having an opening near a bottom of the oil reservoir, and the refrigerant outlet pipe. A structure in which a separating member inclined downward toward the inner surface of the container body is provided on the entire surface of the outer chamber in the horizontal direction near the lower portion of the opening, so that the capacity of the oil reservoir portion can be increased or the oil can be increased. Even if the inner diameter of the container body is increased to increase the cross-sectional area of the separation material for the purpose of improving the separation performance, the inner diameter of the inner chamber for performing centrifugal separation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved. In addition, since the refrigerant inlet pipe is communicated from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet pipe are required, and the number of manufacturing steps can be reduced.

【0015】また、請求項3に記載の発明は、容器本体
の内部上端より下方垂直に設けた下方に向かって径が小
となり下方が開口した所定長さの円錐形状の仕切板によ
り、容器本体内の上部を内側室と外側室に分離し、前記
仕切板より下方を油溜まり部とする。さらに、容器本体
の外側から前記仕切板の接線方向に前記内側室に連通
し、前記内側室内の上部に開口部を有する冷媒入口管
と、容器本体の外側からに前記外側室に連通し、前記外
側室内の上部に開口部を有する冷媒出口管と、容器本体
の外側から前記油溜まり部に連通し、前記油溜まり部の
底部近傍に開口部を有する油排出管と、前記冷媒出口管
の開口部の下方近傍の水平方向に前記外側室全面に容器
本体の内側面に向かって下方に傾斜している分離材を設
ける構造としたことにより、オイル溜まり部の容量の増
加、或いは、油分離性能の向上を目的とした分離材の断
面積の増加のために容器本体の内径を大きくしても、遠
心分離を行う内側室の内径が大きくならない。従って、
冷媒の旋回半径に反比例する遠心力の低下による、油分
離能力の低下を防止できる。また、遠心分離初期段階の
冷媒は、油含有率が高いため油分離が容易であり、弱い
遠心力でも油分離率が高く、また、油含有率が高いため
圧力損失が大きい。そして、遠心分離末期段階の冷媒
は、油含有率が低いため油分離が困難であり、弱い遠心
力では油分離率が低く、また、油含有率が低いため圧力
損失が小さい。従って、遠心分離初期段階は、内径が大
きく冷媒の旋回半径が大きいため圧力損失の小さい内側
室上部で油分離を行うことにより、圧力損失を低減で
き、また、冷媒の油含有率が高いため、旋回半径の増加
により遠心力が弱くなっても油分離率を高く保てる。そ
して、遠心分離末期段階は、内径が小さく冷媒の旋回半
径が小さいため遠心力の強い内側室下部で油分離を行う
ことにより、油分離率の低下を防止でき、また、冷媒の
油含有率が低いため、旋回半径が小さくなっても圧力損
失の増加を防止できる。従って、油分離能力を低下させ
ることなく、圧力損失を低減できる。また、分離材を容
器本体の内側面に向けて下方に傾斜させているため、分
離材に付着したオイルが容器本体の内側面へ流動し、分
離材へのオイルの付着による油分離能力の低下を防止で
き、そして、オイルは容器本体の内側面を伝い油溜まり
部に落下するため、内側室から外側室に向かう冷媒によ
るオイルの再飛散による油分離能力の低下を防止でき、
さらに、分離材の断面積が増加するため分離材通過時の
冷媒の流速が低下し、油分離能力を向上できる。
According to a third aspect of the present invention, the container body is provided with a cone-shaped partition plate having a predetermined length and having a downwardly decreasing diameter and opening downward, which is provided vertically downward from the inner upper end of the container body. The upper part of the inside is separated into an inner chamber and an outer chamber, and an area below the partition plate is an oil reservoir. Further, the refrigerant chamber communicates with the inner chamber in a tangential direction of the partition plate from outside the container body, and a refrigerant inlet pipe having an opening at an upper portion of the inner chamber, and communicates with the outer chamber from outside the container body, A refrigerant outlet pipe having an opening in the upper part of the outer chamber, an oil discharge pipe communicating with the oil reservoir from outside the container body, and having an opening near the bottom of the oil reservoir, and an opening of the refrigerant outlet pipe In the horizontal direction near the lower part of the container, a separating member inclined downward toward the inner surface of the container body is provided on the entire surface of the outer chamber, so that the capacity of the oil reservoir portion is increased or the oil separating performance is increased. Even if the inner diameter of the container body is increased in order to increase the cross-sectional area of the separation material for the purpose of improving the inner diameter, the inner diameter of the inner chamber for centrifugal separation does not increase. Therefore,
It is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Further, the refrigerant in the initial stage of centrifugal separation has a high oil content, so that oil separation is easy, the oil separation rate is high even with a weak centrifugal force, and the pressure loss is large due to the high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult, and the oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high, Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugal separation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the inner diameter is small and the turning radius of the refrigerant is small and the centrifugal force is strong, and the oil content of the refrigerant is reduced. Since it is low, it is possible to prevent an increase in pressure loss even if the turning radius becomes small. Therefore, the pressure loss can be reduced without lowering the oil separation ability. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil falls along the inner surface of the container body and falls into the oil sump, so that it is possible to prevent a decrease in the oil separation capacity due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber,
Further, since the cross-sectional area of the separation material increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.

【0016】また、請求項4に記載の発明は、容器本体
の内部上端より下方垂直に設けた下方に向かって径が小
となり下方が開口した所定長さの円錐形状の仕切板によ
り、容器本体内の上部を内側室と外側室に分離し、前記
仕切板より下方を油溜まり部とする。さらに、容器本体
の上面から前記内側室に連通し、前記内側室内の上部に
前記仕切板の接線方向に冷媒を吐き出す開口部を有する
冷媒入口管と、容器本体の外側から前記外側室に連通
し、前記外側室内の上部に開口部を有する冷媒出口管
と、容器本体の外側から前記油溜まり部に連通し、前記
油溜まり部の底部近傍に開口部を有する油排出管と、前
記冷媒出口管の開口部の下方近傍の水平方向に前記外側
室全面に容器本体の内側面に向かって下方に傾斜してい
る分離材を設ける構造としたことにより、オイル溜まり
部の容量の増加、或いは、油分離性能の向上を目的とし
た分離材の断面積の増加のために容器本体の内径を大き
くしても、遠心分離を行う内側室の内径が大きくならな
い。従って、冷媒の旋回半径に反比例する遠心力の低下
による、油分離能力の低下を防止できる。また、遠心分
離初期段階の冷媒は、油含有率が高いため油分離が容易
であり、弱い遠心力でも油分離率が高く、また、油含有
率が高いため圧力損失が大きい。そして、遠心分離最終
段階の冷媒は、油含有率が低いため油分離が困難であ
り、弱い遠心力では油分離率が低く、また、油含有率が
低いため圧力損失が小さい。従って、遠心分離初期段階
は、内径が大きく冷媒の旋回半径が大きいため圧力損失
の小さい内側室上部で油分離を行うことにより、圧力損
失を低減でき、また、冷媒の油含有率が高いため、旋回
半径の増加により遠心力が弱くなっても油分離率を高く
保てる。そして、遠心分離最終段階は、内径が小さく冷
媒の旋回半径が小さいため遠心力の強い内側室下部で油
分離を行うことにより、油分離率の低下を防止でき、ま
た、冷媒の油含有率が低いため、旋回半径が小さくなっ
ても圧力損失の増加を防止できる。従って、油分離能力
を低下させることなく、圧力損失を低減できる。また、
分離材を容器本体の内側面に向けて下方に傾斜させてい
るため、分離材に付着したオイルが容器本体の内側面へ
流動し、分離材へのオイルの付着による油分離能力の低
下を防止でき、そして、オイルは容器本体の内側面を伝
い油溜まり部に落下するため、内側室から外側室に向か
う冷媒によるオイルの再飛散による油分離能力の低下を
防止でき、さらに、分離材の断面積が増加するため分離
材通過時の冷媒の流速が低下し、油分離能力を向上でき
る。また、冷媒入口管を容器本体の上面から内側室に連
通させたため、冷媒入口管設置のための穴あけ作業及び
溶接作業が1箇所のみであり、製造工数も低減できる。
According to a fourth aspect of the present invention, the container body is provided with a cone-shaped partition plate having a predetermined length and having a downwardly decreasing diameter and being open downward, which is provided vertically downward from the upper end inside the container body. The upper part of the inside is separated into an inner chamber and an outer chamber, and an area below the partition plate is an oil reservoir. Further, a refrigerant inlet pipe communicating with the inner chamber from the upper surface of the container body and having an opening at the upper part of the inner chamber for discharging refrigerant in a tangential direction of the partition plate, and communicating with the outer chamber from outside the container body. A refrigerant outlet pipe having an opening at an upper part in the outer chamber, an oil discharge pipe communicating with the oil reservoir from outside the container body, and having an opening near a bottom of the oil reservoir, and the refrigerant outlet pipe. A structure in which a separating member inclined downward toward the inner surface of the container body is provided on the entire surface of the outer chamber in the horizontal direction near the lower portion of the opening, so that the capacity of the oil reservoir portion can be increased or the oil can be increased. Even if the inner diameter of the container body is increased to increase the cross-sectional area of the separation material for the purpose of improving the separation performance, the inner diameter of the inner chamber for performing centrifugal separation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Further, the refrigerant in the initial stage of centrifugal separation has a high oil content, so that oil separation is easy, the oil separation rate is high even with a weak centrifugal force, and the pressure loss is large due to the high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult. The oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high, Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the centrifugal force is strong because the inner diameter is small and the turning radius of the refrigerant is small, and the oil content of the refrigerant is reduced. Since it is low, it is possible to prevent an increase in pressure loss even if the turning radius becomes small. Therefore, the pressure loss can be reduced without lowering the oil separation ability. Also,
Since the separating material is inclined downward toward the inner surface of the container body, the oil adhering to the separating material flows to the inner surface of the container body, preventing a decrease in oil separation ability due to the oil adhering to the separating material. The oil drops along the inner surface of the container body into the oil reservoir, so that it is possible to prevent a decrease in the oil separation capacity due to the oil re-scattering by the refrigerant flowing from the inner chamber to the outer chamber. Since the area is increased, the flow rate of the refrigerant when passing through the separation material is reduced, and the oil separation ability can be improved. In addition, since the refrigerant inlet pipe is communicated from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet pipe are required, and the number of manufacturing steps can be reduced.

【0017】以下本発明の実施の携帯について図面を参
照しながら説明する。尚、図中の実線の矢印は冷媒の流
れを、点線の矢印は油の流れを示す。
Hereinafter, a mobile phone according to an embodiment of the present invention will be described with reference to the drawings. The solid arrows in the drawing indicate the flow of the refrigerant, and the dotted arrows indicate the flow of the oil.

【0018】(実施の形態1)次に、本発明の実施の形
態1について図1〜図2を用いて説明する。
(Embodiment 1) Next, Embodiment 1 of the present invention will be described with reference to FIGS.

【0019】図1は本発明の実施の形態1における油分
離器の構造図であり、図2は、図1の構造図に示されて
いる断面Aにおける断面図である。容器本体10の上部
は、容器本体10の内部上端から下方垂直に設けた下方
が開口した所定長さの円筒形状の仕切板11により、内
側室12と外側室13に分離される。また、容器本体1
0の内部の仕切板11より下方は油溜まり部14とす
る。15は冷媒入口管であり、容器本体10の外側から
仕切板11の接線方向に内側室12に連通し、内側室1
2内の上部に開口部を有する。16は冷媒出口管であ
り、容器本体10の外側から外側室13に連通し、外側
室13内の上部に開口部を有する。17は油排出口であ
り、容器本体10の外側から油溜まり部14に連通し、
油溜まり部14の底部近傍に開口部を有する。18は分
離材であり、冷媒出口管16の開口部の下方近傍の水平
方向に外側室13の全面に設けられ、仕切板11の円筒
形の中心に向かって下方に傾斜させている。
FIG. 1 is a structural view of an oil separator according to Embodiment 1 of the present invention, and FIG. 2 is a cross-sectional view taken along a section A shown in the structural view of FIG. The upper portion of the container main body 10 is separated into an inner chamber 12 and an outer chamber 13 by a cylindrical partition plate 11 having a predetermined length and having a downward opening and provided vertically downward from the upper end inside the container main body 10. The container body 1
The portion below the partition plate 11 in the inside of the oil reservoir 0 is an oil reservoir 14. Reference numeral 15 denotes a refrigerant inlet pipe, which communicates with the inner chamber 12 in the tangential direction of the partition plate 11 from the outside of the container body 10 to the inner chamber 1.
2 has an opening at the top. Reference numeral 16 denotes a refrigerant outlet pipe, which communicates with the outside chamber 13 from the outside of the container body 10 and has an opening in the upper part of the outside chamber 13. Reference numeral 17 denotes an oil discharge port, which communicates with the oil reservoir 14 from outside the container body 10;
An opening is provided near the bottom of the oil reservoir 14. Reference numeral 18 denotes a separating member, which is provided on the entire surface of the outer chamber 13 in the horizontal direction near the lower portion of the opening of the refrigerant outlet pipe 16 and is inclined downward toward the center of the cylindrical shape of the partition plate 11.

【0020】次に、このように構成された油分離器内の
冷媒及び油の挙動について説明する。まず、圧縮機から
吐出された油を含む気相冷媒は、冷媒入口管15から内
側室12の上部に導かれ、旋回下降流を生成し遠心力に
よって油が分離される。この分離された油は、重力によ
り仕切板11の内側面を伝い下降し、油溜まり部14に
落下する。その後、冷媒は外側室13の下部に導かれ、
分離材18を通過し、外側室13の上部に導かれる。こ
の時、分離材18では冷媒中に含まれる油を捕集するた
め、さらに油が分離される。この分離された油は、重力
により分離材18の傾斜に沿って容器本体10の内側面
に流動し、容器本体10の内側面を伝い、油溜まり部1
4に落下する。その後、冷媒は冷媒出口管16よりサイ
クルに戻される。また、油溜まり部14に落下した油
は、油排出口17より圧縮機の吸入側にもどされる。
Next, the behavior of the refrigerant and the oil in the oil separator configured as described above will be described. First, the gaseous refrigerant containing oil discharged from the compressor is guided from the refrigerant inlet pipe 15 to the upper part of the inner chamber 12, generates a swirling downward flow, and the oil is separated by centrifugal force. The separated oil descends along the inner surface of the partition plate 11 due to gravity, and falls into the oil reservoir 14. Thereafter, the refrigerant is guided to the lower part of the outer chamber 13,
After passing through the separating member 18, it is guided to the upper part of the outer chamber 13. At this time, the oil is further separated by the separating member 18 to collect the oil contained in the refrigerant. The separated oil flows to the inner surface of the container body 10 along the inclination of the separating member 18 due to gravity, travels along the inner surface of the container body 10, and the oil sump 1
Fall to 4. Thereafter, the refrigerant is returned to the cycle through the refrigerant outlet pipe 16. The oil that has fallen into the oil reservoir 14 is returned from the oil outlet 17 to the suction side of the compressor.

【0021】この実施の形態1によれば、オイル溜まり
部の容量の増加、或いは、油分離性能の向上を目的とし
た分離材の断面積の増加のために容器本体の内径を大き
くしても、遠心分離を行う内側室の内径が大きくならな
い。従って、冷媒の旋回半径に反比例する遠心力の低下
による、油分離能力の低下を防止できる。また、分離材
を容器本体の内側面に向けて下方に傾斜させているた
め、分離材に付着したオイルが容器本体の内側面へ流動
し、分離材へのオイルの付着による油分離能力の低下を
防止でき、そして、オイルは容器本体の内側面を伝い油
溜まり部に落下するため、内側室から外側室に向かう冷
媒によるオイルの再飛散による油分離能力の低下を防止
でき、さらに、分離材の断面積が増加するため分離材通
過時の冷媒の流速が低下し、油分離能力を向上できる。
According to the first embodiment, even if the inner diameter of the container body is increased to increase the capacity of the oil reservoir or the cross-sectional area of the separating material for the purpose of improving oil separation performance. The inner diameter of the inner chamber for centrifugation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.

【0022】(実施の形態2)次に、本発明の実施の形
態2について図3〜図4を用いて説明する。
(Embodiment 2) Next, Embodiment 2 of the present invention will be described with reference to FIGS.

【0023】図3は本発明の実施の形態2における油分
離器の構造図であり、図4は、図3の構造図に示されて
いる断面Aにおける断面図である。容積本体10の上部
は、容器本体10の内部上端から下方垂直に設けた下方
が開口した所定長さの円筒形状の仕切板11により、内
側室12と外側室13に分離される。また、容器本体1
0の内部の仕切板11より下方は油溜まり部14とす
る。15は冷媒入口管であり、容器本体10の上面から
内側室12に連通し、内側室12内の上部に仕切板11
の接線方向に冷媒を吐き出す開口部を有する。16は冷
媒出口管であり、容器本体10の外側から外側室13に
連通し、外側室13内の上部に開口部を有する。17は
油排出口であり、容器本体10の外側から油溜まり部1
4に連通し、油溜まり部14の底部近傍に開口部を有す
る。19は分離材であり、冷媒出口管16の開口部の下
方近傍の水平方向に外側室13の全面に設けられ、仕切
板11の円筒形の中心に向かって下方に傾斜させてい
る。
FIG. 3 is a structural view of an oil separator according to Embodiment 2 of the present invention, and FIG. 4 is a cross-sectional view taken along a section A shown in the structural view of FIG. The upper part of the volume main body 10 is separated into an inner chamber 12 and an outer chamber 13 by a cylindrical partition plate 11 having a predetermined length, which is provided vertically downward from the upper end of the inside of the container main body 10 and has an open bottom. The container body 1
The portion below the partition plate 11 in the inside of the oil reservoir 0 is an oil reservoir 14. Reference numeral 15 denotes a refrigerant inlet pipe, which communicates with the inner chamber 12 from the upper surface of the container body 10 and has a partition plate 11
Has an opening for discharging the refrigerant in the tangential direction of. Reference numeral 16 denotes a refrigerant outlet pipe, which communicates with the outside chamber 13 from the outside of the container body 10 and has an opening in the upper part of the outside chamber 13. Reference numeral 17 denotes an oil discharge port.
4 and has an opening near the bottom of the oil reservoir 14. Reference numeral 19 denotes a separating member, which is provided on the entire surface of the outer chamber 13 in the horizontal direction near the opening of the refrigerant outlet pipe 16 and is inclined downward toward the center of the cylindrical shape of the partition plate 11.

【0024】次に、このように構成された油分離器内の
冷媒及び油の挙動について説明する。まず、圧縮機から
吐出された油を含む気相冷媒は、冷媒入口管15から内
側室12の上部に導かれ、旋回下降流を生成し遠心力に
よって油が分離される。この分離された油は、重力によ
り仕切板11の内側面を伝い下降し、油溜まり部14に
落下する。その後、冷媒は外側室13の下部に導かれ、
分離材19を通過し、外側室13の上部に導かれる。こ
の時、分離材19では冷媒中に含まれる油を捕集するた
め、さらに油が分離される。この分離された油は、重力
により分離材19の傾斜に沿って容器本体10の内側面
に流動し、容器本体10の内側面を伝い、油溜まり部1
4に落下する。その後、冷媒は冷媒出口管16よりサイ
クルに戻される。また、油溜まり部14に落下した油
は、油排出口17より圧縮機の吸入側にもどされる。
Next, the behavior of the refrigerant and the oil in the oil separator configured as described above will be described. First, the gaseous refrigerant containing oil discharged from the compressor is guided from the refrigerant inlet pipe 15 to the upper part of the inner chamber 12, generates a swirling downward flow, and the oil is separated by centrifugal force. The separated oil descends along the inner surface of the partition plate 11 due to gravity, and falls into the oil reservoir 14. Thereafter, the refrigerant is guided to the lower part of the outer chamber 13,
After passing through the separating member 19, it is guided to the upper part of the outer chamber 13. At this time, the separating material 19 collects the oil contained in the refrigerant, so that the oil is further separated. The separated oil flows to the inner surface of the container body 10 along the inclination of the separating member 19 due to gravity, and travels along the inner surface of the container body 10 to form the oil reservoir 1
Fall to 4. Thereafter, the refrigerant is returned to the cycle through the refrigerant outlet pipe 16. The oil that has fallen into the oil reservoir 14 is returned from the oil outlet 17 to the suction side of the compressor.

【0025】この実施の形態2によれば、オイル溜まり
部の容量の増加、或いは、油分離性能の向上を目的とし
た分離材の断面積の増加のために容器本体の内径を大き
くしても、遠心分離を行う内側室の内径が大きくならな
い。従って、冷媒の旋回半径に反比例する遠心力の低下
による、油分離能力の低下を防止できる。また、分離材
を容器本体の内側面に向けて下方に傾斜させているた
め、分離材に付着したオイルが容器本体の内側面へ流動
し、分離材へのオイルの付着による油分離能力の低下を
防止でき、そして、オイルは容器本体の内側面を伝い油
溜まり部に落下するため、内側室から外側室に向かう冷
媒によるオイルの再飛散による油分離能力の低下を防止
でき、さらに、分離材の断面積が増加するため分離材通
過時の冷媒の流速が低下し、油分離能力を向上できる。
また、冷媒入口管を容器本体の上面から内側室に連通さ
せたため、冷媒入口管設置のための穴あけ作業及び溶接
作業が1箇所のみであり、製造工数も低減できる。
According to the second embodiment, even if the inner diameter of the container body is increased to increase the capacity of the oil reservoir or the cross-sectional area of the separating material for the purpose of improving oil separation performance. The inner diameter of the inner chamber for centrifugation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.
In addition, since the refrigerant inlet pipe is communicated from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet pipe are required, and the number of manufacturing steps can be reduced.

【0026】(実施の形態3)次に本発明の実施の形態
3について図5〜図6を用いて説明する。
(Embodiment 3) Next, Embodiment 3 of the present invention will be described with reference to FIGS.

【0027】図5や本発明の実施の形態3における油分
離器の構造図であり、図6は、図5の構造図に示されて
いる断面Aにおける断面図である。容器本体10の上部
は、容器本体10の内部上端から下方垂直に設けた下方
に向かって径が小となり下方が開口した所定長さの円錐
形状の仕切板20により、内側室21と外側室22に分
離される。また、容器本体10の内部の仕切板20より
下方は油溜まり部14とする。23は冷媒入口管であ
り、容器本体10の外側から仕切板20の接線方向に内
側室21に連通し、内側室21内の上部に開口部を有す
る。16は冷媒出口管であり、容器本体10の外側から
外側室22に連通し、外側室22内の上部に開口部を有
する。17は油排出口であり、容器本体10の外側から
油溜まり部14に連通し、油溜まり部14の底部近傍に
開口部を有する。24は分離材であり、冷媒出口管16
の開口部の下方近傍の水平方向に外側室22の全面に設
けられ、仕切板20の円錐形の中心に向かって下方に傾
斜させている。
FIG. 5 is a structural view of the oil separator according to the third embodiment of the present invention, and FIG. 6 is a cross-sectional view taken along a cross section A shown in the structural view of FIG. The upper part of the container main body 10 is provided with an inner chamber 21 and an outer chamber 22 by a conical partitioning plate 20 having a predetermined length and having a diameter which decreases downward from the upper end inside the container main body 10 and is open downward. Is separated into Further, the portion below the partition plate 20 inside the container body 10 is an oil reservoir 14. Reference numeral 23 denotes a refrigerant inlet pipe, which communicates with the inner chamber 21 in the tangential direction of the partition plate 20 from the outside of the container body 10 and has an opening in the upper part of the inner chamber 21. Reference numeral 16 denotes a refrigerant outlet pipe, which communicates with the outside chamber 22 from the outside of the container body 10 and has an opening in the upper part of the outside chamber 22. Reference numeral 17 denotes an oil outlet, which communicates with the oil reservoir 14 from outside the container body 10 and has an opening near the bottom of the oil reservoir 14. Reference numeral 24 denotes a separation material, and the refrigerant outlet pipe 16
The partitioning plate 20 is provided on the entire surface of the outer chamber 22 in the horizontal direction near the lower part of the opening, and is inclined downward toward the center of the conical shape of the partition plate 20.

【0028】次に、このように構成された油分離器内の
冷媒及び油の挙動について説明する。まず、圧縮機から
吐出された油を含む気相冷媒は、冷媒入口管23から内
側室21の上部に導かれ、旋回下降流を生成し遠心力に
よって油が分離される。この分離された油は、重力によ
り仕切板20の内側面を伝い下降し、油溜まり部14に
落下する。その後、冷媒は外側室22の下部に導かれ、
分離材24を通過し、外側室22の上部に導かれる。こ
の時、分離材24では冷媒中に含まれる油を捕集するた
め、さらに油が分離される。この分離された油は、重力
により分離材24の傾斜に沿って容器本体10の内側面
に流動し、容器本体10の内側面を伝い、油溜まり部1
4に落下する。その後、冷媒は冷媒出口管16よりサイ
クルに戻される。また、油溜まり部14に落下した油
は、油排出口17より圧縮機の吸入側にもどされる。
Next, the behavior of the refrigerant and the oil in the oil separator configured as described above will be described. First, the gas-phase refrigerant containing oil discharged from the compressor is guided from the refrigerant inlet pipe 23 to the upper part of the inner chamber 21, generates a swirling downward flow, and the oil is separated by centrifugal force. The separated oil descends along the inner surface of the partition plate 20 due to gravity and falls into the oil reservoir 14. Thereafter, the refrigerant is guided to the lower part of the outer chamber 22,
After passing through the separating material 24, it is guided to the upper part of the outer chamber 22. At this time, the oil is further separated by the separating member 24 in order to collect the oil contained in the refrigerant. The separated oil flows to the inner surface of the container body 10 along the inclination of the separating member 24 due to gravity, and travels along the inner surface of the container body 10, and the oil sump 1
Fall to 4. Thereafter, the refrigerant is returned to the cycle through the refrigerant outlet pipe 16. The oil that has fallen into the oil reservoir 14 is returned from the oil outlet 17 to the suction side of the compressor.

【0029】この実施の形態3によれば、オイル溜まり
部の容量の増加、或いは、油分離性能の向上を目的とし
た分離材の断面積の増加のために容器本体の内径を大き
くしても、遠心分離を行う内側室の内径が大きくならな
い。従って、冷媒の旋回半径に反比例する遠心力の低下
による、油分離能力の低下を防止できる。また、遠心分
離初期段階の冷媒は、油含有率が高いため油分離が容易
であり、弱い遠心力でも油分離率が低く、また、油含有
率が高いため圧力損失が大きい。そして、遠心分離末期
段階の冷媒は、油含有率が低いため油分離が困難であ
り、弱い遠心力では油分離率が低く、また、油含有率が
低いため圧力損失が小さい。従って、遠心分離初期段階
は、内径が大きく冷媒の旋回半径が大きいため圧力損失
の小さい内側室上部で油分離を行うことにより、圧力損
失を低減でき、また、冷媒の油含有率が高いため、旋回
半径の増加により遠心力が弱くなっても油分離率を高く
保てる。そして、遠心分離末期段階は、内径が小さく冷
媒の旋回半径が小さいため遠心力の強い内側室下部で油
分離を行うことにより、油分離率の低下を防止でき、ま
た、冷媒の油含有率が低いため、旋回半径が小さくなっ
ても圧力損失の増加を防止できる。従って、油分離能力
を低下させることなく、圧力損失を低減できる。また、
分離材を容器本体の内側面に向けて下方に傾斜させてい
るため、分離材に付着したオイルが容器本体の内側面へ
流動し、分離材へのオイルの付着による油分離能力の低
下を防止でき、そして、オイルは容器本体の内側面を伝
い油溜まり部に落下するため、内側室から外側室に向か
う冷媒によるオイルの再飛散による油分離能力の低下を
防止でき、さらに、分離材の断面積が増加するため分離
材通過時の冷媒の流速が低下し、油分離能力を向上でき
る。
According to the third embodiment, even if the inner diameter of the container body is increased to increase the capacity of the oil reservoir or the cross-sectional area of the separating material for the purpose of improving oil separation performance. The inner diameter of the inner chamber for centrifugation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Further, the refrigerant in the initial stage of centrifugal separation has a high oil content, so that oil separation is easy, the oil separation rate is low even with a weak centrifugal force, and the pressure loss is high due to the high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult, and the oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high, Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugal separation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the inner diameter is small and the turning radius of the refrigerant is small and the centrifugal force is strong, and the oil content of the refrigerant is reduced. Since it is low, it is possible to prevent an increase in pressure loss even if the turning radius becomes small. Therefore, the pressure loss can be reduced without lowering the oil separation ability. Also,
Since the separating material is inclined downward toward the inner surface of the container body, the oil adhering to the separating material flows to the inner surface of the container body, preventing a decrease in oil separation ability due to the oil adhering to the separating material. The oil drops along the inner surface of the container body into the oil reservoir, so that it is possible to prevent a decrease in the oil separation capacity due to the oil re-scattering by the refrigerant flowing from the inner chamber to the outer chamber. Since the area is increased, the flow rate of the refrigerant when passing through the separation material is reduced, and the oil separation ability can be improved.

【0030】(実施の形態4)次に本発明の実施の形態
4について図7〜図8を用いて説明する。
(Embodiment 4) Next, Embodiment 4 of the present invention will be described with reference to FIGS.

【0031】図7は本発明の実施の形態4における油分
離器の構造図であり、図8は、図7の構造図に示されて
いる断面Aにおける断面図である。容器本体10の上部
は、容器本体10の内部上端から下方垂直に設けた下方
に向かって径が小となり下方が開口した所定長さの円錐
形状の仕切板20により、内側室21と外側室22に分
離される。また、容器本体10の内部の仕切板20より
下方は油溜まり部14とする。23は冷媒入口管であ
り、容器本体10の上面から内側室21に連通し、内側
室21内の上部に仕切板20の接線方向に冷媒を吐き出
す開口部を有する。16は冷媒出口管であり、容器本体
10の外側から外側室22に連通し、外側室22内の上
部に開口部を有する。17は油排出口であり、容器本体
10の外側から油溜まり部14に連通し、油溜まり部1
4の底部近傍に開口部を有する。25は分離材であり、
冷媒出口管16の開口部の下方近傍の水平方向に外側室
22の全面に設けられ、仕切板20の円錐形の中心に向
かって下方に傾斜させている。
FIG. 7 is a structural view of an oil separator according to Embodiment 4 of the present invention, and FIG. 8 is a cross-sectional view taken along a cross-section A shown in the structural view of FIG. The upper part of the container main body 10 is provided with an inner chamber 21 and an outer chamber 22 by a conical partitioning plate 20 having a predetermined length and having a diameter which decreases downward from the upper end inside the container main body 10 and is open downward. Is separated into Further, the portion below the partition plate 20 inside the container body 10 is an oil reservoir 14. Reference numeral 23 denotes a refrigerant inlet pipe, which communicates with the inner chamber 21 from the upper surface of the container body 10 and has an opening in the upper part of the inner chamber 21 for discharging refrigerant in a tangential direction of the partition plate 20. Reference numeral 16 denotes a refrigerant outlet pipe, which communicates with the outside chamber 22 from the outside of the container body 10 and has an opening in the upper part of the outside chamber 22. Reference numeral 17 denotes an oil discharge port, which communicates with the oil reservoir 14 from outside the container body 10 and
4 has an opening near the bottom. 25 is a separating material,
The partition wall 20 is provided on the entire surface of the outer chamber 22 in the horizontal direction near the lower portion of the opening of the refrigerant outlet pipe 16 and is inclined downward toward the center of the conical shape of the partition plate 20.

【0032】次に、このように構成された油分離器内の
冷媒及び油の挙動について説明する。まず、圧縮機から
吐出された油を含む気相冷媒は、冷媒入口管23から内
側室21の上部に導かれ、旋回下降流を生成し遠心力に
よって油が分離される。この分離された油は、重力によ
り仕切板20の内側面を伝い、油溜まり部14に落下す
る。その後、冷媒は外側室22の下部に導かれ、分離材
25を通過し、外側室22の上部に導かれる。この時、
分離材25では冷媒中に含まれる油を捕集するため、さ
らに油が分離される。この分離された油は、重力により
分離材25の傾斜に沿って容器本体10の内側面に流動
し、容器本体10の内側面を伝い、油溜まり部14に落
下する。その後、冷媒は冷媒出口管16よりサイクルに
戻される。また、油溜まり部14に落下した油は、油排
出口17より圧縮機の吸入側にもどされる。
Next, the behavior of the refrigerant and the oil in the oil separator configured as described above will be described. First, the gas-phase refrigerant containing oil discharged from the compressor is guided from the refrigerant inlet pipe 23 to the upper part of the inner chamber 21, generates a swirling downward flow, and the oil is separated by centrifugal force. The separated oil travels along the inner surface of the partition plate 20 due to gravity and falls into the oil reservoir 14. Thereafter, the refrigerant is guided to the lower part of the outer chamber 22, passes through the separating material 25, and is guided to the upper part of the outer chamber 22. At this time,
In the separating material 25, oil contained in the refrigerant is collected, so that the oil is further separated. The separated oil flows to the inner surface of the container body 10 along the inclination of the separating material 25 due to gravity, and travels down the inner surface of the container body 10 to drop into the oil reservoir 14. Thereafter, the refrigerant is returned to the cycle through the refrigerant outlet pipe 16. The oil that has fallen into the oil reservoir 14 is returned from the oil outlet 17 to the suction side of the compressor.

【0033】この実施の形態4によれば、オイル溜まり
部の容量の増加、或いは、油分離性能の向上を目的とし
た分離材の断面積の増加のために容器本体の内径を大き
くしても、遠心分離を行う内側室の内径が大きくならな
い。従って、冷媒の旋回半径に反比例する遠心力の低下
による、油分離能力の低下を防止できる。また、遠心分
離初期段階の冷媒は、油含有率が高いため油分離が容易
であり、弱い遠心力でも油分離率が高く、また、油含有
率が高いため圧力損失が大きい。そして、遠心分離最終
段階の冷媒は、油含有率が低いため油分離が困難であ
り、弱い遠心力では油分離率が低く、また、油含有率が
低いため圧力損失が小さい。従って、遠心分離初期段階
は、内径が大きく冷媒の旋回半径が大きいため圧力損失
の小さい内側室上部で油分離を行うことにより、圧力損
失を低減でき、また、冷媒の油含有率が高いため、旋回
半径の増加により遠心力が弱くなっても油分離率を高く
保てる。そして、遠心分離最終段階は、内径が小さく冷
媒の旋回半径が小さいため遠心力の強い内側室下部で油
分離を行うことにより、油分離率の低下を防止でき、ま
た、冷媒の油含有率が低いため、旋回半径が小さくなっ
ても圧力損失の増加を防止できる。従って、油分離能力
を低下させることなく、圧力損失を低減できる。また、
分離材を容器本体の内側面に向けて下方に傾斜させてい
るため、分離材に付着したオイルが容器本体の内側面へ
流動し、分離材へのオイルの付着による油分離能力の低
下を防止でき、そして、オイルは容器本体の内側面を伝
い油溜まり部に落下するため、内側室から外側室に向か
う冷媒によるオイルの再飛散による油分離能力の低下を
防止でき、さらに、分離材の断面積が増加するため分離
材通過時の冷媒の流速が低下し、油分離能力を向上でき
る。また、冷媒入口管を容器本体の上面から内側室に通
過させたため、冷媒入口管設置のための穴あけ作業及び
溶接作業が1箇所のみであり、製造工数も低減できる。
According to the fourth embodiment, even if the inner diameter of the container body is increased to increase the capacity of the oil reservoir or the cross-sectional area of the separating material for the purpose of improving oil separation performance. The inner diameter of the inner chamber for centrifugation does not increase. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Further, the refrigerant in the initial stage of centrifugal separation has a high oil content, so that oil separation is easy, the oil separation rate is high even with a weak centrifugal force, and the pressure loss is large due to the high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult. The oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high, Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the centrifugal force is strong because the inner diameter is small and the turning radius of the refrigerant is small, and the oil content of the refrigerant is reduced. Since it is low, it is possible to prevent an increase in pressure loss even if the turning radius becomes small. Therefore, the pressure loss can be reduced without lowering the oil separation ability. Also,
Since the separating material is inclined downward toward the inner surface of the container body, the oil adhering to the separating material flows to the inner surface of the container body, preventing a decrease in oil separation ability due to the oil adhering to the separating material. The oil drops along the inner surface of the container body into the oil reservoir, so that it is possible to prevent a decrease in the oil separation capacity due to the oil re-scattering by the refrigerant flowing from the inner chamber to the outer chamber. Since the area is increased, the flow rate of the refrigerant when passing through the separation material is reduced, and the oil separation ability can be improved. Further, since the refrigerant inlet pipe is passed from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet pipe are required, and the number of manufacturing steps can be reduced.

【0034】[0034]

【発明の効果】以上のように本発明は、容器本体の内部
上端より下方垂直に設けた下方が開口した所定長さの円
筒形状の仕切板と、仕切板により容器本体内の上部を内
側室と外側室に分離し、仕切板より下方を油溜まり部と
するとともに、容器本体の外側から仕切板の接線方向に
内側室に連通し、内側室内の上部に開口部を有する冷媒
入口管と、容器本体の外側からに外側室に連通し、外側
室内の上部に開口部を有する冷媒出口管と、容器本体の
外側から油溜まり部に連通し、油溜まり部の底部近傍に
開口部を有する油排出管と、冷媒出口管の開口部の下方
近傍の水平方向に外側室全面に前記仕切板の円筒形の中
心に向かって下方に傾斜している分離材を設けた構造と
したものである。そのため、オイル溜まり部の容量の増
加、或いは、油分離性能の向上を目的とした分離材の断
面積の増加のために容器本体の内径を大きくしても、遠
心分離を行う内側室の内径が大きくならない。従って、
冷媒の旋回半径に反比例する遠心力の低下による、油分
離能力の低下が防止できる。また、分離材を容器本体の
内側室に向けて下方に傾斜させているため、分離材に付
着したオイルが容器本体の内側面へ流動し、分離材への
オイルの付着による油分離能力の低下を防止でき、そし
て、オイルは容器本体の内側面を伝い油溜まり部に落下
するため、内側室から外側室に向かう冷媒によるオイル
の再飛散による油分離能力の低下を防止でき、さらに、
分離材の断面積が増加するため分離材通過時の冷媒の流
速が低下し、油分離能力を向上できる。
As described above, according to the present invention, there is provided a cylindrical partition plate having a predetermined length, which is provided vertically below the upper end of the inside of the container body and has a downwardly opened lower part, and the upper portion of the inside of the container body being formed by the partition plate by the inner chamber. And a refrigerant inlet pipe having an oil sump below the partition plate and communicating with the inner chamber in the tangential direction of the partition plate from the outside of the container body, and having an opening at the upper part of the inner chamber, A refrigerant outlet pipe communicating from the outside of the container body to the outer chamber and having an opening at the top inside the outer chamber; and an oil communicating with the oil reservoir from the outside of the container body and having an opening near the bottom of the oil reservoir. The separator has a structure in which a discharge pipe and a separating member inclined downward toward the center of the cylindrical shape of the partition plate are provided on the entire outer chamber in the horizontal direction near the opening of the refrigerant outlet pipe. Therefore, even if the inner diameter of the inner chamber for centrifugal separation is increased even if the inner diameter of the container body is increased due to an increase in the capacity of the oil reservoir or an increase in the cross-sectional area of the separation material for the purpose of improving the oil separation performance, Does not grow. Therefore,
A decrease in oil separation capacity due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant can be prevented. In addition, since the separating material is inclined downward toward the inner chamber of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil falls along the inner surface of the container body and falls into the oil reservoir, so that it is possible to prevent a decrease in the oil separation capability due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber,
Since the cross-sectional area of the separation material increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.

【0035】また、容器本体の内部上端より下方垂直に
設けた下方が開口した所定長さの円筒形状の仕切板と、
仕切板により容器本体内の上部を内側室と外側室に分離
し、仕切板より下方を油溜まり部とするとともに、容器
本体の上面から内側室に連通し、内側室内の上部に仕切
板の接線方向に冷媒を吐き出す開口部を有する冷媒入口
管と、容器本体の外側からに外側室に連通し、外側室内
の上部に開口部を有する冷媒出口管と、容器本体の外側
から油溜まり部に連通し、油溜まり部の底部近傍に開口
部を有する油排出管と、冷媒出口管の開口部の下方近傍
の水平方向に外側室全面に前記仕切板の円筒形の中心に
向かって下方に傾斜している分離材を設けた構造とした
ものである。そのため、オイル溜まり部の容量の増加、
或いは、油分離性能の向上を目的とした分離材の断面積
の増加のために容器本体の内径を大きくしても、遠心分
離を行う内側室の内径が大きくならない。従って、冷媒
の旋回半径に反比例する遠心力の低下による、油分離能
力の低下が防止できる。また、分離材を容器本体の内側
面に向けて下方に傾斜させているため、分離材に付着し
たオイルが容器本体の内側面へ流動し、分離材へのオイ
ルの付着による油分離能力の低下を防止でき、そして、
オイルは容器本体の内側面を伝い油溜まり部に落下する
ため、内側室から外側室に向かう冷媒によるオイルの再
飛散による油分離能力の低下を防止でき、さらに、分離
材の断面積が増加するため分離材通過時の冷媒の流速が
低下し、油分離能力を向上できる。また、冷媒入口菅を
容器本体の上面から内側室に連通させたため、冷媒入口
管設置のための穴あけ作業及び溶接作業が1箇所のみで
あり、製造工数も低減できる。
A cylindrical partition plate having a predetermined length and having an opening at a lower portion provided vertically below the upper end of the inside of the container body;
A partition plate separates the upper part of the inside of the container body into an inner chamber and an outer chamber, and the lower part of the partition plate serves as an oil sump, and communicates with the inner chamber from the upper surface of the container body. A refrigerant inlet pipe having an opening for discharging refrigerant in a direction, a refrigerant outlet pipe having an opening at an upper portion of the outer chamber from the outside of the container main body, and communicating with an oil reservoir from the outside of the container main body. And an oil discharge pipe having an opening near the bottom of the oil sump, and a slope inclined downward toward the center of the cylindrical shape of the partition plate over the entire outer chamber in the horizontal direction near the bottom of the opening of the refrigerant outlet pipe. This is a structure in which a separating material is provided. As a result, the capacity of the oil reservoir increases,
Alternatively, even if the inner diameter of the container body is increased to increase the cross-sectional area of the separation material for the purpose of improving oil separation performance, the inner diameter of the inner chamber for centrifugal separation does not increase. Therefore, it is possible to prevent a decrease in oil separation capability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. Can be prevented, and
Since the oil travels down the inner surface of the container body and falls into the oil sump, it is possible to prevent a decrease in the oil separation capacity due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber, and further increase the cross-sectional area of the separating material. Therefore, the flow velocity of the refrigerant when passing through the separating material is reduced, and the oil separation ability can be improved. Further, since the refrigerant inlet tube is communicated from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet tube are required, and the number of manufacturing steps can be reduced.

【0036】また、容器本体の内部上端より下方垂直に
設けた下方に向かって径が小となり下方が開口した所定
長さの円錐形状の仕切板と、仕切板により容器本体内の
上部を内側室と外側室に分離し、仕切板より下方を油溜
まり部とするとともに、容器本体の外側から仕切板の接
線方向に内側室に連通し、内側室内の上部に開口部を有
する冷媒入口管と、容器本体の外側からに外側室に連通
し、外側室内の上部に開口部を有する冷媒出口管と、容
器本体の外側から油溜まり部に連通し、油溜まり部の底
部近傍に開口部を有する油排出管と、冷媒出口管の開口
部の下方近傍の水平方向に外側室全面に仕切板の円錐形
の中心に向かって下方に傾斜している分離材を設けた構
造としたものである。そのため、オイル溜まり部の容量
の増加、或いは、油分離性能の向上を目的とした分離材
の断面積の増加のために容器本体の内径を大きくして
も、遠心分離を行う内側室の内径が大きくならない。従
って、冷媒の旋回半径に反比例する遠心力の低下によ
る、油分離能力の低下を防止できる。また、遠心分離初
期段階の冷媒は、油含有率が高いため油分離が容易であ
り、弱い遠心力でも油分離率が高く、また、油含有率が
高いため圧力損失が大きい。そして、遠心分離末期段階
の冷媒は、油含有率が低いため油分離が困難であり、弱
い遠心力では油分離率が低く、また、油含有率が低いた
め圧力損失が小さい。従って、遠心分離初期段階は、内
径が大きく冷媒の旋回半径が大きいため圧力損失の小さ
い内側室上部で油分離を行うことにより、圧力損失を低
減でき、また、冷媒の油含有率が高いため、旋回半径の
増加により遠心力が弱くなっても油分離率を高く保て
る。そして、遠心分離末期段階は、内径が小さく冷媒の
旋回半径が小さいため遠心力の強い内側室下部で油分離
を行うことにより、油分離率の低下を防止でき、また、
冷媒の油含有率が低いため、旋回半径が小さくなっても
圧力損失の増加を防止できる。従って、油分離能力を低
下させることなく、圧力損失を低減できる。また、分離
材を容器本体の内側面に向けて下方に傾斜させているた
め、分離材に付着したオイルが容器本体の内側面に流動
し、分離材へのオイルの付着による油分離能力の低下を
防止でき、そして、オイルは容器本体の内側面を伝い油
溜まり部に落下するため、内側室から外側室に向かう冷
媒によるオイルの再飛散による油分離能力の低下を防止
でき、さらに、分離材の断面積が増加するため分離材通
過時の冷媒の流速が低下し、油分離能力を向上できる。
Further, a conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a smaller diameter and is open downward, is provided below the upper end of the container body by the partition plate. And a refrigerant inlet pipe having an oil sump below the partition plate and communicating with the inner chamber in the tangential direction of the partition plate from the outside of the container body, and having an opening at the upper part of the inner chamber, A refrigerant outlet pipe communicating from the outside of the container body to the outer chamber and having an opening at the top inside the outer chamber; and an oil communicating with the oil reservoir from the outside of the container body and having an opening near the bottom of the oil reservoir. The discharge pipe and the separating member inclined downward toward the center of the conical shape of the partition plate are provided on the entire outer chamber in the horizontal direction near the lower part of the opening of the refrigerant outlet pipe. Therefore, even if the inner diameter of the inner chamber for centrifugal separation is increased even if the inner diameter of the container body is increased due to an increase in the capacity of the oil reservoir or an increase in the cross-sectional area of the separation material for the purpose of improving the oil separation performance, Does not grow. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Further, the refrigerant in the initial stage of centrifugal separation has a high oil content, so that oil separation is easy, the oil separation rate is high even with a weak centrifugal force, and the pressure loss is large due to the high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult, and the oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high, Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugal separation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the inner diameter is small and the turning radius of the refrigerant is small, so that the centrifugal force is strong.
Since the oil content of the refrigerant is low, an increase in pressure loss can be prevented even when the turning radius is reduced. Therefore, the pressure loss can be reduced without lowering the oil separation ability. In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved.

【0037】また、容器本体の内部上端より下方垂直に
設けた下方に向かって径が小となり下方が開口した所定
長さの円錐形状の仕切板と、仕切板により容器本体内の
上部を内側室と外側室に分離し、仕切板より下方を油溜
まり部とするとともに、容器本体の上面から内側室に連
通し、内側室内の上部に仕切板の接線方向に冷媒を吐き
出す開口部を有する冷媒入口管と、容器本体の外側から
に外側室に連通し、外側室内の上部に開口部を有する冷
媒出口管と、容器本体の外側から油溜まり部に連通し、
油溜まり部の底部近傍に開口部を有する油排出管と、冷
媒出口管の開口部の下方近傍の水平方向に外側室全面に
仕切板の円錐形の中心に向かって下方に傾斜している分
離材を設けた構造としたものである。そのため、オイル
溜まり部の容量の増加、或いは、油分離性能の向上を目
的とした分離材の断面積の増加のために容器本体の内径
を大きくしても、遠心分離を行う内側室の内径が大きく
ならない。従って、冷媒の旋回半径に反比例する遠心力
の低下による、油分離能力の低下を防止できる。また、
遠心分離初期段階の冷媒は、油含有率が高いため油分離
が容易であり、弱い遠心力でも油分離率が高く、また、
油含有率が高いため圧力損失が大きい。そして、遠心分
離最終段階の冷媒は、油含有率が低いため油分離が困難
であり、弱い遠心力では油分離率が低く、また、油含有
率が低いため圧力損失が小さい。従って、遠心分離初期
段階は、内径が大きく冷媒の旋回半径が大きいため圧力
損失の小さい内側室上部で油分離を行うことにより、圧
力損失を低減でき、また、冷媒の油含有率が高いため、
旋回半径の増加により遠心力が弱くなっても油分離率を
高く保てる。そして、遠心分離最終段階は、内径が小さ
く冷媒の旋回半径が小さいため遠心力の強い内側室下部
で油分離を行うことにより、油分離率の低下を防止で
き、また、冷媒の油含有率が低いため、旋回半径が小さ
くなっても圧力損失の増加を防止できる。従って、油分
離能力を低下させることなく、圧力損失を低減できる。
また、分離材を容器本体の内側面に向けて下方に傾斜さ
せているため、分離材に付着したオイルが容器本体の内
側面へ流動し、分離材へのオイルの付着による油分離能
力の低下を防止でき、そして、オイルは容器本体の内側
面を伝い油溜まり部に落下するため、内側室から外側室
に向かう冷媒によるオイルの再飛散による油分離能力の
低下を防止でき、さらに、分離材の断面積が増加するた
め分離材通過時の冷媒の流速が低下し、油分離能力を向
上できる。また、冷媒入口管を容器本体の上面から内側
室に連通させたため、冷媒入口管設置のための穴あけ作
業及び溶接作業が1箇所のみであり、製造工数も低減で
きる。
Further, a conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a smaller diameter and is open downward, is provided below the upper end of the container body by the partition plate. A refrigerant inlet having an oil reservoir below the partition plate, communicating with the inner chamber from the upper surface of the container body, and having an opening in the upper portion of the inner chamber for discharging refrigerant in a tangential direction of the partition plate. A pipe and a refrigerant outlet pipe having an opening at an upper portion of the outer chamber from the outside of the container main body, and a refrigerant outlet pipe from the outside of the container main body,
An oil discharge pipe having an opening near the bottom of the oil reservoir, and a separation inclined downward toward the center of the conical shape of the partition plate over the entire outer chamber in the horizontal direction near the bottom of the opening of the refrigerant outlet pipe. This is a structure provided with materials. Therefore, even if the inner diameter of the inner chamber for centrifugal separation is increased even if the inner diameter of the container body is increased due to an increase in the capacity of the oil reservoir or an increase in the cross-sectional area of the separation material for the purpose of improving the oil separation performance, Does not grow. Therefore, it is possible to prevent a decrease in oil separation ability due to a decrease in centrifugal force that is inversely proportional to the turning radius of the refrigerant. Also,
The refrigerant in the initial stage of centrifugation has a high oil content, so that oil separation is easy, and even at low centrifugal force, the oil separation rate is high,
High pressure loss due to high oil content. The refrigerant in the final stage of centrifugal separation has a low oil content, so that oil separation is difficult. The oil separation rate is low with a weak centrifugal force, and the pressure loss is low because the oil content is low. Therefore, in the initial stage of centrifugal separation, by performing oil separation in the upper part of the inner chamber where the internal diameter is large and the turning radius of the refrigerant is large and the pressure loss is small, the pressure loss can be reduced, and since the oil content of the refrigerant is high,
Even if the centrifugal force is weakened by increasing the turning radius, the oil separation rate can be kept high. In the final stage of centrifugation, the oil separation rate can be prevented from lowering by performing oil separation in the lower part of the inner chamber where the centrifugal force is strong because the inner diameter is small and the turning radius of the refrigerant is small, and the oil content of the refrigerant is reduced. Since it is low, it is possible to prevent an increase in pressure loss even if the turning radius becomes small. Therefore, the pressure loss can be reduced without lowering the oil separation ability.
In addition, since the separating material is inclined downward toward the inner surface of the container body, oil adhering to the separating material flows to the inner surface of the container body, and the oil separating ability is reduced due to the adhesion of the oil to the separating material. And the oil drops along the inner surface of the container body to the oil sump, so that the oil separating ability can be prevented from lowering due to the re-scattering of the oil by the refrigerant flowing from the inner chamber to the outer chamber. Since the cross-sectional area of the refrigerant increases, the flow velocity of the refrigerant when passing through the separation material decreases, and the oil separation ability can be improved. In addition, since the refrigerant inlet pipe is communicated from the upper surface of the container body to the inner chamber, only one drilling operation and welding operation for installing the refrigerant inlet pipe are required, and the number of manufacturing steps can be reduced.

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

【図1】本発明の実施の形態1における油分離器の構造
FIG. 1 is a structural diagram of an oil separator according to a first embodiment of the present invention.

【図2】本発明の実施の形態1における油分離器の断面
FIG. 2 is a cross-sectional view of the oil separator according to the first embodiment of the present invention.

【図3】本発明の実施の形態2における油分離器の構造
FIG. 3 is a structural diagram of an oil separator according to a second embodiment of the present invention.

【図4】本発明の実施の形態2における油分離器の断面
FIG. 4 is a sectional view of an oil separator according to a second embodiment of the present invention.

【図5】本発明の実施の形態3における油分離器の構造
FIG. 5 is a structural diagram of an oil separator according to a third embodiment of the present invention.

【図6】本発明の実施の形態3における油分離器の断面
FIG. 6 is a sectional view of an oil separator according to a third embodiment of the present invention.

【図7】本発明の実施の形態4における油分離器の構造
FIG. 7 is a structural diagram of an oil separator according to Embodiment 4 of the present invention.

【図8】本発明の実施の形態4における油分離器の断面
FIG. 8 is a sectional view of an oil separator according to a fourth embodiment of the present invention.

【図9】従来の油分離器の構造図FIG. 9 is a structural diagram of a conventional oil separator.

【符号の説明】[Explanation of symbols]

10 容器本体 11 仕切板 12 内側室 13 外側室 14 油溜まり部 15 冷媒入口管 16 冷媒出口管 17 油排出管 18 分離材 19 分離材 20 仕切板 21 内側室 22 外側室 23 冷媒入口管 24 分離材 25 分離材 DESCRIPTION OF SYMBOLS 10 Container main body 11 Partition plate 12 Inner chamber 13 Outer chamber 14 Oil reservoir 15 Refrigerant inlet pipe 16 Refrigerant outlet pipe 17 Oil discharge pipe 18 Separating material 19 Separating material 20 Partition plate 21 Inner chamber 22 Outer chamber 23 Refrigerant inlet pipe 24 Separating material 25 Separation materials

───────────────────────────────────────────────────── フロントページの続き (72)発明者 日下 道美 大阪府東大阪市高井田本通4丁目2番5号 松下冷機株式会社内 ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Michimi Kusaka 4-5-2-5 Takaidahondori, Higashiosaka-shi, Osaka Matsushita Refrigeration Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 容器本体の内部上端より下方垂直に設け
た下方が開口した所定長さの円筒形状の仕切板と、前記
仕切板により容器本体内の上部を内側室と外側室に分離
し、前記仕切板より下方を油溜まり部とするとともに、
容器本体の外側から前記仕切板の接線方向に前記内側室
に連通し、前記内側室内の上部に開口部を有する冷媒入
口管と、容器本体の外側から前記外側室に連通し、前記
外側室内の上部に開口部を有する冷媒出口管と、容器本
体の外側から前記油溜まり部に連通し、前記油溜まり部
の底部近傍に開口部を有する油排出管と、前記冷媒出口
管の開口部の下方近傍の水平方向に前記外側室全面に容
器本体の内側面に向かって下方に傾斜している分離材を
設けた油分離器。
1. A cylindrical partition plate having a predetermined length, which is provided vertically downward from an upper end of the inside of a container main body and has a lower opening, and an upper part in the container main body is separated into an inner chamber and an outer chamber by the partition plate. A portion below the partition plate is an oil reservoir,
A refrigerant inlet pipe communicating from the outside of the container body to the inner chamber in a tangential direction of the partition plate and having an opening at an upper portion of the inner chamber, and communicating with the outer chamber from the outside of the container body to the inside of the outer chamber. A refrigerant outlet pipe having an opening at an upper portion, an oil discharge pipe communicating with the oil reservoir from outside the container body, and having an opening near a bottom of the oil reservoir, and an opening below the refrigerant outlet pipe. An oil separator provided with a separating member which is inclined downward toward the inner surface of the container body over the entire outer chamber in the vicinity of the horizontal direction.
【請求項2】 容器本体の内部上端より下方垂直に設け
た下方が開口した所定長さの円筒形状の仕切板と、前記
仕切板により容器本体内の上部を内側室と外側室に分離
し、前記仕切板より下方を油溜まり部とするとともに、
容器本体の上面から前記内側室に連通し、前記内側室内
の上部に前記仕切板の接線方向に冷媒を吐き出す開口部
を有する冷媒入口管と、容器本体の外側から前記外側室
に連通し、前記外側室内の上部に開口部を有する冷媒出
口管と、容器本体の外側から前記油溜まり部に連通し、
前記油溜まり部の底部近傍に開口部を有する油排出管
と、前記冷媒出口管の開口部の下方近傍の水平方向に前
記外側室全面に容器本体の内側面に向かって下方に傾斜
している分離材を設けた油分離器。
2. A cylindrical partition plate having a predetermined length and having a downwardly opened lower portion provided vertically below an inner upper end of the container body, and an upper portion inside the container body is separated into an inner chamber and an outer chamber by the partition plate. A portion below the partition plate is an oil reservoir,
A refrigerant inlet pipe communicating with the inner chamber from the upper surface of the container main body and having an opening for discharging refrigerant in a tangential direction of the partition plate at an upper part of the inner chamber, and communicating with the outer chamber from outside the container main body; A refrigerant outlet pipe having an opening in the upper part of the outer chamber, and communicating with the oil reservoir from outside the container body,
An oil discharge pipe having an opening in the vicinity of the bottom of the oil reservoir, and a horizontal direction near the bottom of the opening of the refrigerant outlet pipe, which is inclined downward toward the inner surface of the container body over the entire outer chamber in the horizontal direction. Oil separator with separation material.
【請求項3】 容器本体の内部上端より下方垂直に設け
た下方に向かって径が小となり下方が開口した所定長さ
の円錐形状の仕切板と、前記仕切板により容器本体内の
上部を内側室と外側室に分離し、前記仕切板より下方を
油溜まり部とするとともに、容器本体の外側から前記仕
切板の接線方向に前記内側室に連通し、前記内側室内の
上部に開口部を有する冷媒入口管と、容器本体の外側か
ら前記外側室に連通し、前記外側室内の上部に開口部を
有する冷媒出口管と、容器本体の外側から前記油溜まり
部に連通し、前記油溜まり部の底部近傍に開口部を有す
る油排出管と、前記冷媒出口管の開口部の下方近傍の水
平方向に前記外側室全面に容器本体の内側面に向かって
下方に傾斜している分離材を設けた油分離器。
3. A conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a downwardly decreasing diameter and opens downward, and an upper part inside the container body is inwardly provided by the partition plate. The partition is separated into a chamber and an outer chamber, and a portion below the partition plate is used as an oil sump portion, and communicates from the outside of the container body to the inner chamber in a tangential direction of the partition plate, and has an opening at an upper portion of the inner chamber. A refrigerant inlet pipe, a refrigerant outlet pipe communicating from the outside of the container body to the outer chamber and having an opening in an upper part of the outer chamber, and a refrigerant outlet pipe communicating from the outside of the container body to the oil sump; An oil discharge pipe having an opening in the vicinity of the bottom and a separating material inclined downward toward the inner surface of the container body are provided on the entire surface of the outer chamber in the horizontal direction near the lower part of the opening of the refrigerant outlet pipe. Oil separator.
【請求項4】 容器本体の内部上端より下方垂直に設け
た下方に向かって径が小となり下方が開口した所定長さ
の円錐形状の仕切板と、前記仕切板により容器本体内の
上部を内側室と外側室に分離し、前記仕切板より下方を
油溜まり部とするとともに、容器本体の上面から前記内
側室に連通し、前記内側室内の上部に前記仕切板の接線
方向に冷媒を吐き出す開口部を有する冷媒入口管と、容
器本体の外側から前記外側室に連通し、前記外側室内の
上部に開口部を有する冷媒出口管と、容器本体の外側か
ら前記油溜まり部に連通し、前記油溜まり部の底部近傍
に開口部を有する油排出管と、前記冷媒出口管の開口部
の下方近傍の水平方向に前記外側室全面に容器本体の内
側面に向かって下方に傾斜している分離材を設けた油分
離器。
4. A conical partition plate of a predetermined length, which is provided vertically downward from the upper end of the inside of the container body and has a smaller diameter and opens downward at the lower side, and the upper part inside the container body is inwardly provided by the partition plate. An opening which is separated into a chamber and an outer chamber, and has an oil reservoir below the partition plate, communicates with the inner chamber from the upper surface of the container body, and discharges refrigerant in an upper part of the inner chamber in a tangential direction of the partition plate. A refrigerant inlet pipe having a portion, a refrigerant outlet pipe communicating from the outside of the container body to the outer chamber, and a refrigerant outlet pipe having an opening in an upper portion of the outer chamber; An oil discharge pipe having an opening near the bottom of the reservoir, and a separating member inclined downwardly toward the inner surface of the container body over the entire outer chamber in the horizontal direction near the bottom of the opening of the refrigerant outlet pipe. Oil separator provided.
JP17607396A 1996-07-05 1996-07-05 Oil separator Pending JPH1019423A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17607396A JPH1019423A (en) 1996-07-05 1996-07-05 Oil separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17607396A JPH1019423A (en) 1996-07-05 1996-07-05 Oil separator

Publications (1)

Publication Number Publication Date
JPH1019423A true JPH1019423A (en) 1998-01-23

Family

ID=16007255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17607396A Pending JPH1019423A (en) 1996-07-05 1996-07-05 Oil separator

Country Status (1)

Country Link
JP (1) JPH1019423A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2101894A1 (en) * 2006-11-30 2009-09-23 Westlake Longview Corporation High-pressure separator
JP2012241963A (en) * 2011-05-18 2012-12-10 Fuji Electric Co Ltd Gas-liquid separator
WO2024029028A1 (en) * 2022-08-04 2024-02-08 三菱電機株式会社 Oil separator and refrigeration cycle device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2101894A1 (en) * 2006-11-30 2009-09-23 Westlake Longview Corporation High-pressure separator
JP2010511492A (en) * 2006-11-30 2010-04-15 ウエストレイク ロングビュー コーポレイション High pressure separator
JP2012241963A (en) * 2011-05-18 2012-12-10 Fuji Electric Co Ltd Gas-liquid separator
WO2024029028A1 (en) * 2022-08-04 2024-02-08 三菱電機株式会社 Oil separator and refrigeration cycle device

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