JPH06235572A - Oil separator of refrigerating plant - Google Patents
Oil separator of refrigerating plantInfo
- Publication number
- JPH06235572A JPH06235572A JP2236893A JP2236893A JPH06235572A JP H06235572 A JPH06235572 A JP H06235572A JP 2236893 A JP2236893 A JP 2236893A JP 2236893 A JP2236893 A JP 2236893A JP H06235572 A JPH06235572 A JP H06235572A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- refrigerant gas
- separated
- separation
- separating
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/02—Centrifugal separation of gas, liquid or oil
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
【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しられてお
り、このものは図１４に示したように、密閉容器５１の
上部に冷媒ガス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状分離板５４が垂直に取り付け
られ冷媒ガス５５ａは入口管５２から入り、円筒５４内
側上部から下部側に流れ円筒状分離板５４の下側を通り
冷媒ガス５５ａは上部の出口管５３から吐出ガス５ｂは
外へ吐出される。冷媒ガス５５ａに含まれているミスト
状の油は、円筒状分離板５４の内側を通過している時に
油の自重により分離され油５６は下部に溜る。密閉容器
５１の底には、油戻し管５５がある。そして、この種の
従来構造の油分離器は、処理速度が早くなると冷媒ガス
５５ａは分離され溜っている油表面に衝突し再飛散が発
生し冷媒ガス５５ａは微粒子の油を持ち去るために分離
効率が低下する構造となっている。この種の構造は、処
理流速の比較的遅い条件に限られており適用が困難な構
造である。2. Description of the Related Art Heretofore, as an oil separator of this type, Japanese Patent Laid-Open No.
As shown in FIG. 14, a structure such as that of Japanese Patent Laid-Open No. 60-106516 is well-known. As shown in FIG. Cylindrical separation plates 54 for vertically separating the oil are connected to the insides of the closed container 51, and the refrigerant gas 55a enters from the inlet pipe 52 and flows from the inside of the cylinder 54 to the lower side. The refrigerant gas 55a passes through the lower side and the discharge gas 5b is discharged to the outside from the upper outlet pipe 53. The mist-like oil contained in the refrigerant gas 55a is separated by its own weight while passing through the inside of the cylindrical separation plate 54, and the oil 56 is accumulated in the lower part. At the bottom of the closed container 51, there is an oil return pipe 55. In the conventional oil separator of this type, when the processing speed increases, the refrigerant gas 55a collides with the separated oil surface and re-scatters, and the refrigerant gas 55a carries away fine particle oil to separate the oil. Is a structure that decreases. This type of structure is difficult to apply because it is limited to the condition that the processing flow rate is relatively slow.
【０００３】[0003]
【発明が解決しようとする課題】ところで図１４に示す
油分離器の従来技術では、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５５
ａ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
下部に落とす分離機構である。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。効率を上げるためには、大きな形状にしなけれ
ばならない欠点があった。冷凍装置内の油が多くなると
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り冷凍装置の信頼性が低下する。本
発明の目的は、小形で構造が容易で処理流速が変化して
も分離性能の高い機構を提供することにある。By the way, in the prior art of the oil separator shown in FIG. 14, the refrigerant gas 55 enters the closed container 51 through the refrigerant gas inlet pipe 52 and the cylindrical separation plate 54.
When the oil contained in a 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 specific gravity is larger than that of the refrigerant gas. Oil is a separation mechanism that drops it to the bottom. However, when the processing flow rate is relatively high, the efficiency is rapidly decreased only by the separation by centrifugation. In order to improve efficiency, there is a drawback that a large shape must be used. If the amount of oil in the refrigeration system increases, the performance of the heat exchanger will deteriorate and the expansion valve and control valve will malfunction, resulting in a reduction in the reliability of the refrigeration system. An object of the present invention is to provide a mechanism that is small in size, has a simple structure, and has high separation performance even when the processing flow rate changes.
【０００４】[0004]
【課題を解決するための手段】本発明の分離機構は、冷
媒ガスは分離器上部の入口管を介し水平方向に入り円筒
形状の分離板の表面に当てて分離し、その後は冷媒ガス
通路にデミスタを設置し、衝突，拡散，膨張により油を
分離する機構で、デミスタの取付け位置は分離した油を
冷媒ガスは押し出す方向、つまり、内容積が小さな室か
ら大きな室になるようにすることにより、デミスタ内に
油の溜りが起きない最適構造にすることにより処理流速
が早くなっても冷媒ガスが油面に当たらない分離機構と
する。処理流速が早い場合の冷媒ガスでも、衝突による
分離効率は低下しない。衝突を利用した分離機構は処理
流速が早くなっても分離効率の低下はないので、デミス
タの最適な構造の組合わせにより分離効率の高い機構に
より達成出来る。According to the separation mechanism of the present invention, the refrigerant gas enters in the horizontal direction through the inlet pipe in the upper part of the separator and is applied to the surface of the cylindrical separation plate to separate it. It is a mechanism that installs a demister and separates oil by collision, diffusion and expansion. The mounting position of the demister is the direction in which the separated gas is pushed out by the refrigerant gas, that is, by changing the internal volume from a small chamber to a large chamber. By adopting an optimal structure in which oil does not accumulate in the demister, a separation mechanism is provided in which the refrigerant gas does not hit the oil surface even if the processing flow rate becomes faster. Even when the processing gas has a high processing flow rate, the separation efficiency due to collision does not decrease even with the refrigerant gas. Since the separation mechanism utilizing collision does not lower the separation efficiency even if the processing flow speed becomes faster, it can be achieved by a mechanism having a high separation efficiency by combining the optimal structure of the demister.
【０００５】[0005]
【作用】圧縮機の高圧の吐出冷媒ガスは、油分離器上部
の吐出管を介して水平に入り円筒形状の分離板に当た
り、ここで大部分の油は分離される。次に、デミスタ内
を通過する際に、衝突，膨張、及び拡散作用などでによ
り微粒子の油を分離する。分離された冷媒ガスは、筒形
状の分離板の内側を流れ上部に進み出口管より外へ出
る。一方、分離された油は底部に溜り、底に設けた油戻
し管を介して、圧縮機内に戻す。油戻し管は、ここでは
２本示しているが何本でもよい。The high-pressure refrigerant gas discharged from the compressor enters horizontally through the discharge pipe above the oil separator and hits the cylindrical separation plate, where most of the oil is separated. Next, when passing through the inside of the demister, the fine particle oil is separated by collision, expansion, and diffusion. The separated refrigerant gas flows through the inside of the cylindrical separation plate, goes to the upper part, and exits from the outlet pipe. On the other hand, the separated oil collects at the bottom and returns to the inside of the compressor through an oil return pipe provided at the bottom. Two oil return pipes are shown here, but any number may be used.
【０００６】[0006]
【実施例】以下、本発明の一実地例を図１により説明す
る。図２，図３，図４，図５，図６，図７，図８，図
９，図１０，図１１，図１２、及び図１３は幾つかの応
用例を示し、図１４は従来構造を示す。図１に本発明の
一実地例に係る油分離器の全体側面図を示す。１は本
体、２は入口管、３は出口管、４は支え足、５は円筒形
状の分離板、５ａは分離板５の固定部、６と８は油戻し
管、７と９は金網形状のフィルタ、１０は油面を示す。
矢印は冷媒ガスの流れ方向を示し、ａは冷媒ガス、ｂは
吐出ガスを示す。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、矢印のように吸
入管２からは本体１内に入り分離板５に衝突し、ここで
大部分の油は分離され下部に落ちる。分離板５は円筒形
をしているので、冷媒ガスａは表面の外形を両側から周
り反対側の位置で冷媒ガスａ同士が衝突し油がさらに分
離される。分離された冷媒ガスａは、矢印に示すように
分離板５の下側を流れ、分離板５の内側を通り上部の出
口管３から外へ吐出ガスｂが吐出される。分離板５が容
易な形状をしているが、油５が分離され落ちる方向と冷
媒ガスの進む方向が異なっており処理流速が早くなって
も、油面１０には影響しないので再飛散の現象は発生に
ない。したがって、処理流速の広い範囲で分離効率の性
能がよい。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A practical example of the present invention will be described below with reference to FIG. FIGS. 2, 3, 4, 5, 5, 6, 7, 8, 9, 10, 11, 12, and 13 show some application examples, and FIG. 14 shows a conventional structure. Indicates. FIG. 1 shows an overall side view of an oil separator according to a practical example of the present invention. 1 is a main body, 2 is an inlet pipe, 3 is an outlet pipe, 4 is a supporting leg, 5 is a cylindrical separating plate, 5a is a fixing portion of the separating plate 5, 6 and 8 are oil return pipes, and 7 and 9 are wire mesh-shaped Filter 10 indicates an oil level.
The arrow indicates the flow direction of the refrigerant gas, a indicates the refrigerant gas, and b indicates the discharge gas. 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 refrigeration system enters the main body 1 from the suction pipe 2 and collides with the separation plate 5 as shown by the arrow, and most of the oil is It separates and falls to the bottom. Since the separation plate 5 has a cylindrical shape, the refrigerant gas a surrounds the outer shape of the surface from both sides, and the refrigerant gases a collide with each other at positions on the opposite side to further separate the oil. The separated refrigerant gas a flows under the separation plate 5 as shown by the arrow, passes through the inside of the separation plate 5, and the discharge gas b is discharged from the upper outlet pipe 3 to the outside. The separation plate 5 has an easy shape, but the oil surface 10 is not affected even if the processing flow velocity increases because the direction in which the oil 5 is separated and the direction in which the refrigerant gas advances are different, so the phenomenon of re-scattering occurs. Does not occur. Therefore, the performance of the separation efficiency is good in a wide range of the processing flow rate.
【０００７】次に、油分離器の応用例を図２を用いて説
明する。図１に示した実地例と基本的は同じ分離機構で
あり、異なるところは分離板５ａの上部が本体１から離
れて下部側で支える構造で入口管２は分離板５ｂの片側
を貫通し、反対側の内壁に衝突させる機構にした分離構
造である。次に、分離動作について説明する。冷媒ガス
ａは入口管２から入り分離板５ｂの内壁に衝突し油を分
離する。分離板５ｂの上部は遮蔽されているので、冷媒
ガスａは、下部側に流れるものや円周方向に流れてから
下部側に流れ、冷媒ガス通路５ｃを通り上部出口管から
外へ出る分離機構である。この分離機構は、遠心力を利
用して分離するものと、衝突による分離する構造で分離
効率の高い機構である。ここでは図に示してないが、分
離板５ｂの内壁や天井の壁に小さい穴を数個明けたり絞
り機構つけた穴を付けることにより分離性能は良くな
る。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as the practical example shown in FIG. 1, except that the upper part of the separation plate 5a is separated from the main body 1 and supported on the lower side, and the inlet pipe 2 penetrates one side of the separation plate 5b. It is a separation structure that has a mechanism to collide with the inner wall on the opposite side. Next, the separating operation will be described. The refrigerant gas a enters from the inlet pipe 2 and collides with the inner wall of the separation plate 5b to separate oil. Since the upper part of the separation plate 5b is shielded, the refrigerant gas a flows to the lower side or flows in the circumferential direction and then to the lower side, and then passes through the refrigerant gas passage 5c to come out from the upper outlet pipe to the outside. Is. This separation mechanism has a structure that separates by utilizing centrifugal force and a structure that separates by collision and has high separation efficiency. Although not shown in the figure here, the separation performance is improved by making several small holes in the inner wall of the separation plate 5b or the wall of the ceiling and providing holes with a diaphragm mechanism.
【０００８】次に、油分離器の応用例を図３を用いて説
明する。図２に示した実地例と基本的に全く同じ分離機
構であり、異なるところは入口管２先端部の内側にデミ
スタ２ａを備えることによりデミスタ２ａを通過する際
に油の粒子が膨張，拡散により大きく発達して衝突板に
衝突するので分離効果がよくなり分離効率が向上する。
図３に示してないが、分離板５ｂの内側に緩衝材を設け
ることにより、再飛散が防止され分離効率が向上する。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as the practical example shown in FIG. 2, except that the demister 2a is provided inside the tip of the inlet pipe 2 so that the oil particles expand and diffuse when passing through the demister 2a. Since it greatly develops and collides with the collision plate, the separation effect is improved and the separation efficiency is improved.
Although not shown in FIG. 3, by providing a cushioning material inside the separation plate 5b, re-scattering is prevented and the separation efficiency is improved.
【０００９】次に、油分離器の応用例を図４を用いて説
明する。図２に示した実地例と基本的に全く同じ分離機
構であり、異なるところは分離板５ｂの底面にデミスタ
５ｄを備えることにより微粒子状の油を完全に分離する
ことが出来るので分離効率が向上する。分離機構は、油
の落る方向と冷媒ガスａの流れる方向が同じでありデミ
スタ５ｄ部内に油が溜らないので分離が良くなり、さら
には冷媒ガスａは油の落ちる方向と反対の上部方向に進
ので分離効率が良くなる。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as that of the practical example shown in FIG. 2, except that a demister 5d is provided on the bottom surface of the separation plate 5b, so that fine oil particles can be completely separated, so that the separation efficiency is improved. To do. In the separation mechanism, the direction in which the oil falls and the direction in which the refrigerant gas a flows are the same, and the oil does not accumulate in the demister 5d, resulting in good separation. Further, the refrigerant gas a moves in the upper direction opposite to the direction in which the oil falls. Since it advances, the separation efficiency improves.
【００１０】次に、油分離器の応用例を図５を用いて説
明する。図３及び図４に示した実施例を組み合わせた分
離機構であり、冷媒ガスａの入口管２の先端部の内側に
デミスタ２ａ備え、さらに、分離板５ｂの底面にデミス
タ５ｄを備えることにより、デミスタ２ａ及びデミスタ
５ｄ内の油は冷媒ガスａで押し出されるので、必ず下部
に落ちる。分離機構部が比較的小な寸法でも分離効率の
高い分離機構を備えている。Next, an application example of the oil separator will be described with reference to FIG. 3 and 4, which is a combination of the embodiments shown in FIGS. 3 and 4, in which the demister 2a is provided inside the tip of the inlet pipe 2 for the refrigerant gas a, and the demister 5d is provided on the bottom surface of the separation plate 5b, Since the oil in the demister 2a and the demister 5d is pushed out by the refrigerant gas a, it always drops to the lower part. The separation mechanism has a separation mechanism with high separation efficiency even if the separation mechanism has a relatively small size.
【００１１】次に、油分離器の応用例を図６を用いて説
明する。図２に示した実施例と分離機構は基本的に同じ
であり、冷媒ガスａの入口管２の先端部が上部方向に向
う構造で、分離板５ｂの天井遮蔽板に冷媒ガスを衝突さ
せる機構としたもので、衝突による分離を良くした構造
であり分離効率の高い分離機構を備えている。２は入口
管、５ｂは分離板、そして、５ｃは冷媒ガス通路。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as that of the embodiment shown in FIG. 2, and the tip of the inlet pipe 2 for the refrigerant gas a is directed upward, and the mechanism for causing the refrigerant gas to collide with the ceiling shielding plate of the separation plate 5b. It has a structure that improves separation by collision and is equipped with a separation mechanism with high separation efficiency. 2 is an inlet pipe, 5b is a separating plate, and 5c is a refrigerant gas passage.
【００１２】次に、油分離器の応用例を図７を用いて説
明する。図６に示した実施例と分離機構は基本的に同じ
であり、異なるところは冷媒ガスａの入口管２の先端部
の内側にデミスタ２ａを備えた構造で、冷媒ガスａに含
まれる油は、ここのデミスタ２ａ部を通過することによ
り、微粒子状の油が大きく発達してから衝突するので衝
突効果を向上させたものである。５ｃは冷媒ガスａ通路
であり本体１と分離板５ｂの間を通過し出口管３から外
へ出る。構造が容易で油の分離を良くした分離効率の高
い分離機構を備えている。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as that of the embodiment shown in FIG. 6, except that the structure is provided with a demister 2a inside the tip portion of the inlet pipe 2 for the refrigerant gas a, and the oil contained in the refrigerant gas a is By passing through the demister 2a portion, the fine particle oil is greatly developed and then collides, so that the collision effect is improved. A refrigerant gas a passage 5c passes between the main body 1 and the separation plate 5b and exits from the outlet pipe 3. It has a separation mechanism with a simple structure and good oil separation, and high separation efficiency.
【００１３】次に、油分離器の応用例を図８を用いて説
明する。図６に示した実施例と分離機構は基本的に同じ
であり、異なるところは分離板５ｂの底面にデミスタ５
ｄを備えた構造で、冷媒ガスａに含まれる油は、分離板
５ｂの天井遮蔽板の所で衝突により分離されその後デミ
スタ部５ｅを通過する事により、微粒子状の油が拡散，
膨張の繰り返しにより大きく発達し、自重により下部に
落ちる。５ｃは冷媒ガス通路であり本体１と分離板５ｂ
の間を通過し出口管３から外へ出る。構造が容易で油の
分離を良くした分離効率の高い分離機構を備えている。Next, an application example of the oil separator will be described with reference to FIG. The separating mechanism is basically the same as that of the embodiment shown in FIG. 6, except that the demister 5 is provided on the bottom surface of the separating plate 5b.
In the structure provided with d, the oil contained in the refrigerant gas a is separated by collision at the ceiling shielding plate of the separation plate 5b and then passes through the demister section 5e, so that the fine particle oil diffuses,
It develops greatly due to repeated expansion, and falls to the bottom due to its own weight. Reference numeral 5c is a refrigerant gas passage, which is the main body 1 and the separation plate 5b.
It passes through the space between the outlet pipe 3 and the outside. It has a separation mechanism with a simple structure and good oil separation, and high separation efficiency.
【００１４】次に、油分離器の応用例を図９を用いて説
明する。図７及び図８に示した実施例の組合わせ分離機
構であり基本的には同じである。したがって、分離機構
の動作についての説明は省く。この油分離機構は、分離
効率が高くしかも比較的寸法が小さく出来ると共に、分
離性能の高い分離機構である。Next, an application example of the oil separator will be described with reference to FIG. The combination separating mechanism of the embodiments shown in FIGS. 7 and 8 is basically the same. Therefore, the description of the operation of the separating mechanism is omitted. This oil separation mechanism has high separation efficiency, can be relatively small in size, and has high separation performance.
【００１５】次に、油分離器の応用例を図１０を用いて
説明する。図９に示した実施例と分離機構は基本的には
同じであり、入口配管２の先端部が下向きとなった構造
で、デミスタ部で分離した油は、必ず冷媒ガスで下部に
落す構造になっているのでデミスタ部の目づまりは発生
しないので油分離器の冷媒ガス通過圧力損失は小さい。
衝突板１５は、冷媒ガスａが油面１５に当らないように
したものであり、15ａは油の通路である。衝突板１５が
なくても良い。動作は図９に示した構造と同じであり説
明は省く。Next, an application example of the oil separator will be described with reference to FIG. The separation mechanism is basically the same as that of the embodiment shown in FIG. 9, and the inlet pipe 2 has a structure in which the tip end portion is directed downward, and the oil separated in the demister portion is always dropped to the bottom by the refrigerant gas. Therefore, the clogging of the demister section does not occur, and the refrigerant gas passage pressure loss in the oil separator is small.
The collision plate 15 prevents the refrigerant gas a from hitting the oil surface 15, and 15a is an oil passage. The collision plate 15 may be omitted. The operation is the same as the structure shown in FIG. 9, and the description is omitted.
【００１６】次に、油分離器の応用例を図１１を用いて
説明する。図１に示した実施例と分離機構は基本的には
同じであり、異なるところは、本体１と分離板５との間
にデミスタ５ｅを備え分離板５の外周を冷媒ガスａを回
し遠心力で分離効果を高め遠心力により分離すると共
に、分離された油はデミスタ５ｅ部を通過する際、本体
１の壁面を伝わって油は落ちる。また、デミスタ５ｅを
冷媒ガスが通過する際に油を分離する効果があるので、
構造が容易であるが分離効率が高い。Next, an application example of the oil separator will be described with reference to FIG. The separating mechanism is basically the same as that of the embodiment shown in FIG. 1, except that a demister 5e is provided between the main body 1 and the separating plate 5 to rotate the refrigerant gas a around the outer periphery of the separating plate 5 and to apply centrifugal force. The separating effect is enhanced by the centrifugal force, and the separated oil is transmitted along the wall surface of the main body 1 when passing through the demister 5e portion, and the oil drops. In addition, when the refrigerant gas passes through the demister 5e, it has an effect of separating oil,
The structure is simple, but the separation efficiency is high.
【００１７】次に、油分離器の応用例を図１２及び図１
３を用いて説明する。図１に示した実施例と分離機構は
基本的には同じであり、異なるところは、入口管の先端
部が上向きにした構造で、その他は全く同じである。図
１３に示した図は、図１２のＡ−Ａ断面図を示したもの
で、入口配管２は分離板５の円形の内部側に入った構造
で、冷媒ガスａは分離板５の固定部５ａを旋回して遠心
力による分離機構が入った油分離機構である。ここで
は、分離板５外円形内に入口配管２の先端が入っている
がスペースが十分にある場合は入らなくてもよい。Next, application examples of the oil separator are shown in FIGS. 12 and 1.
3 will be used for the explanation. The separating mechanism is basically the same as that of the embodiment shown in FIG. 1, except that the inlet pipe has a tip portion directed upward, and the other parts are exactly the same. The drawing shown in FIG. 13 is a cross-sectional view taken along the line AA of FIG. 12, in which the inlet pipe 2 enters the circular inner side of the separation plate 5, and the refrigerant gas a is the fixed portion of the separation plate 5. 5a is an oil separation mechanism that swivels 5a and includes a separation mechanism by centrifugal force. Here, the tip of the inlet pipe 2 is included in the outer circle of the separation plate 5, but it may not be included if there is sufficient space.
【００１８】[0018]
【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。
本発明の分離機構は、処理流速の変化に対して分離性能
は影響しない。容易な構造であり、小形，安価に出来
る。According to the present invention, in the separation performance of the oil separator, which has been a drawback so far, the rotational speed changes due to the capacity control of the compressor, so that the discharge amount of the refrigerant gas changes and the oil separation. The processing flow rate of the vessel 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 of the present invention does not affect the separation performance with respect to changes in the processing flow rate. It has a simple structure and can be made small and inexpensive.
【図１】本発明の一実施例である油分離器の全体構造の
断面図。FIG. 1 is a cross-sectional view of the overall structure of an oil separator that is an embodiment of the present invention.
【図２】本発明の第二実施例である油分離器の全体構造
の断面図。FIG. 2 is a sectional view of the overall structure of an oil separator that is a second embodiment of the present invention.
【図３】本発明の第三実施例である油分離器の全体構造
の断面図。FIG. 3 is a sectional view of the overall structure of an oil separator that is a third embodiment of the present invention.
【図４】本発明の第四実施例である油分離器の全体構造
の断面図。FIG. 4 is a sectional view of the overall structure of an oil separator that is a fourth embodiment of the present invention.
【図５】本発明の第五実施例である油分離器の全体構造
の断面図。FIG. 5 is a sectional view of the overall structure of an oil separator that is a fifth embodiment of the present invention.
【図６】本発明の第六実施例である油分離器の全体構造
の断面図。FIG. 6 is a sectional view of the overall structure of an oil separator that is a sixth embodiment of the present invention.
【図７】本発明の第七実施例である油分離器の全体構造
の断面図。FIG. 7 is a sectional view of the overall structure of an oil separator that is a seventh embodiment of the present invention.
【図８】本発明の第八実施例である油分離器の全体構造
の断面図。FIG. 8 is a sectional view of the entire structure of an oil separator that is an eighth embodiment of the present invention.
【図９】本発明の第九実施例である油分離器の全体構造
の断面図。FIG. 9 is a sectional view of the overall structure of an oil separator that is a ninth embodiment of the present invention.
【図１０】本発明の第十実施例である油分離器の全体構
造の断面図。FIG. 10 is a sectional view of the overall structure of an oil separator that is a tenth embodiment of the present invention.
【図１１】本発明の第十一実施例である油分離器の全体
構造の断面図。FIG. 11 is a sectional view of the overall structure of an oil separator that is an eleventh embodiment of the present invention.
【図１２】本発明の第十二実施例である油分離器の全体
構造の断面図。FIG. 12 is a sectional view of the overall structure of an oil separator that is a twelfth embodiment of the present invention.
【図１３】図１２の断面図。13 is a sectional view of FIG.
【図１４】従来の全体構造図の断面図。FIG. 14 is a sectional view of a conventional overall structural view.
１…本体、２…入口管、２ａ…デミスタ、３…出口管、
４…支え足、５…円筒形状の分離板、５ａ…分離板の固
定部、５ｂ…分離板、５ｃ…冷媒ガス通路、５ｄ…デミ
スタ、５ｅ…デミスタ、６，８…油戻し管、７，９…金
網状のフィルタ、１０…油面。1 ... Main body, 2 ... Inlet pipe, 2a ... Demister, 3 ... Outlet pipe,
4 ... Support legs, 5 ... Cylindrical separation plate, 5a ... Separation plate fixing part, 5b ... Separation plate, 5c ... Refrigerant gas passage, 5d ... Demister, 5e ... Demister, 6, 8 ... Oil return pipe, 7, 9 ... Wire mesh filter, 10 ... Oil surface.
───────────────────────────────────────────────────── フロントページの続き (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 (72)発明者 山田 眞朗 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 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kenji Togusa Kenji Togusa 390 Muramatsu, Shimizu City, Shizuoka Prefecture Inside the Shimizu Plant, Hitachi, Ltd. (72) Masaro Yamada 390 Muramatsu, Shimizu City, Shizuoka Hitachi, Ltd. Shimizu Plant, Hitachi Within
Claims (1)
媒ガス内に含まれるミスト状の油を分離する縦形の油分
離器で、上部が分離機構、下部は油溜めの組合わせ構造
で前記冷媒ガスは前記分離機構に水平方向に入り、上部
から吐出される分離構造において、分離板の円筒容器は
本体上部内側に保持され、前記冷媒ガスは前記円筒容器
の外壁に衝突し油を下部に落すと共に遠心により分離し
前記冷媒ガスは前記円筒容器の下側から内側に進んで上
部から外に吐出され分離効率の高い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. A vertical oil separator for separating mist-like oil contained in a high-pressure refrigerant gas discharged from a compressor of a refrigeration system, wherein the upper part is a separating mechanism and the lower part is a combination structure of an oil sump. In the separation structure in which the refrigerant gas enters the separating mechanism in the horizontal direction and is discharged from the upper portion, the cylindrical container of the separating plate is held inside the upper portion of the main body, and the refrigerant gas collides with the outer wall of the cylindrical container to lower the oil. An oil separator of a refrigerating apparatus, which is equipped with a mechanism having a high separation efficiency, in which the refrigerant gas is dropped into the inside of the cylindrical container and is separated by centrifugation, and the refrigerant gas is discharged from the upper part to the outer part from the lower part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2236893A JPH06235572A (en) | 1993-02-10 | 1993-02-10 | Oil separator of refrigerating plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2236893A JPH06235572A (en) | 1993-02-10 | 1993-02-10 | Oil separator of refrigerating plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06235572A true JPH06235572A (en) | 1994-08-23 |
Family
ID=12080696
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2236893A Pending JPH06235572A (en) | 1993-02-10 | 1993-02-10 | Oil separator of refrigerating plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06235572A (en) |
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|---|---|---|---|---|
| JP2007154830A (en) * | 2005-12-07 | 2007-06-21 | Aisin Seiki Co Ltd | Gas liquid separation device for compressor |
| JP2007532853A (en) * | 2004-04-08 | 2007-11-15 | ヨーク・インターナショナル・コーポレーション | Flash tank for use in an economizer circuit |
| US7690216B2 (en) | 2004-11-25 | 2010-04-06 | Lg Electronics Inc. | Oil separator for air conditioners |
| US7967901B2 (en) | 2008-04-14 | 2011-06-28 | Kobe Steel, Ltd. | Lubricating liquid separator |
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-
1993
- 1993-02-10 JP JP2236893A patent/JPH06235572A/en active Pending
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007532853A (en) * | 2004-04-08 | 2007-11-15 | ヨーク・インターナショナル・コーポレーション | Flash tank for use in an economizer circuit |
| US7690216B2 (en) | 2004-11-25 | 2010-04-06 | Lg Electronics Inc. | Oil separator for air conditioners |
| JP2007154830A (en) * | 2005-12-07 | 2007-06-21 | Aisin Seiki Co Ltd | Gas liquid separation device for compressor |
| US7967901B2 (en) | 2008-04-14 | 2011-06-28 | Kobe Steel, Ltd. | Lubricating liquid separator |
| JP2013031798A (en) * | 2011-08-02 | 2013-02-14 | Hino Motors Ltd | Catch tank for air dryer apparatus |
| WO2014020837A1 (en) * | 2012-07-30 | 2014-02-06 | Motohashi Takao | Gas-liquid separation device for air discharge means |
| JP2013210188A (en) * | 2013-06-19 | 2013-10-10 | Mitsubishi Electric Corp | Cyclone oil separator, and compression refrigerating device and air compression device equipped with the same |
| CN104848615A (en) * | 2014-02-13 | 2015-08-19 | 松下知识产权经营株式会社 | Oil separator |
| KR20150095550A (en) * | 2014-02-13 | 2015-08-21 | 파나소닉 아이피 매니지먼트 가부시키가이샤 | Oil separator |
| EP2910875A1 (en) * | 2014-02-13 | 2015-08-26 | Panasonic Intellectual Property Management Co., Ltd. | Oil separator |
| JP2015166668A (en) * | 2014-02-13 | 2015-09-24 | パナソニックＩｐマネジメント株式会社 | oil separator |
| CN104848615B (en) * | 2014-02-13 | 2019-05-14 | 松下知识产权经营株式会社 | Oil eliminator |
| CN112361357A (en) * | 2020-10-21 | 2021-02-12 | 江苏旭龙环境科技有限公司 | Pipeline viscous oil processing apparatus of waste gas paint |
| CN112361357B (en) * | 2020-10-21 | 2023-08-04 | 江苏旭龙环境科技有限公司 | Pipeline oil sticking treatment device for waste gas paint |
| WO2022121432A1 (en) * | 2020-12-08 | 2022-06-16 | 合肥美的暖通设备有限公司 | Oil separator and outdoor unit of air conditioner |
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