JPH0120697B2 - - Google Patents
Info
- Publication number
- JPH0120697B2 JPH0120697B2 JP19551981A JP19551981A JPH0120697B2 JP H0120697 B2 JPH0120697 B2 JP H0120697B2 JP 19551981 A JP19551981 A JP 19551981A JP 19551981 A JP19551981 A JP 19551981A JP H0120697 B2 JPH0120697 B2 JP H0120697B2
- Authority
- JP
- Japan
- Prior art keywords
- oil return
- ejector
- oil
- bypass
- compressor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 28
- 239000007788 liquid Substances 0.000 claims description 17
- 238000005057 refrigeration Methods 0.000 claims description 15
- 230000001105 regulatory effect Effects 0.000 description 5
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- F25B2341/00—Details of ejectors not being used as compression device; Details of flow restrictors or expansion valves
- F25B2341/001—Ejectors not being used as compression device
- F25B2341/0016—Ejectors for creating an oil recirculation
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
Description
【発明の詳細な説明】
本発明は、圧縮機を用いた冷凍装置において、
低圧部分の冷媒に混入した油を圧縮機に戻す装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a refrigeration system using a compressor.
This relates to a device that returns oil mixed in refrigerant in a low pressure section to a compressor.
例えば従来のスクリユー圧縮機を用いた冷凍装
置において第1図に示す如く、スクリユー圧縮機
1、凝縮器15、蒸発器17、吐出管31,3
2、出口管33、蒸気管42、吸入管30により
冷凍サイクルが形成されている冷凍機において、
蒸発器17に溜つた油をスクリユー圧縮機1に戻
すために、吐出管31より吸入管30までをバイ
パス管40,41にて接続し、これらのバイパス
管よりなるバイパス経路中にエゼクタ14を設
け、エゼクタ14の吸入部38と蒸発器17とを
油戻し管37で接続してある。蒸発器17の油を
含んだ冷媒液は、バイパス管40,41の流れに
よりエゼクタ14に吸い込まれ吸入管30を経て
スクリユー圧縮機1に戻される。尚16は膨張弁
である。 For example, in a refrigeration system using a conventional screw compressor, as shown in FIG.
2. In a refrigerator in which a refrigeration cycle is formed by an outlet pipe 33, a steam pipe 42, and an intake pipe 30,
In order to return the oil accumulated in the evaporator 17 to the screw compressor 1, the discharge pipe 31 to the suction pipe 30 are connected by bypass pipes 40, 41, and the ejector 14 is provided in the bypass path formed by these bypass pipes. , the suction section 38 of the ejector 14 and the evaporator 17 are connected by an oil return pipe 37. The oil-containing refrigerant liquid in the evaporator 17 is sucked into the ejector 14 by the flow through the bypass pipes 40 and 41 and returned to the screw compressor 1 via the suction pipe 30. Note that 16 is an expansion valve.
しかしこのような構造の従来のものにおいては
スクリユー圧縮機で吐出圧迄加圧した冷媒ガスを
再び吸込側に戻して吸入せしめるため、冷凍サイ
クルに対しては役に立たない無駄な圧縮仕事が増
加して効率の低下を招く欠点を直していた。本発
明は、エコノマイザーにて蒸発器に入る冷媒液を
冷却し、蒸発した後の、中間圧冷媒ガスの一部を
取り出してエゼクタを介して圧縮機の吸入側に導
き、このエゼクタにより低圧系統中の油を含んだ
冷媒液を吸引してロータ作用空間に戻すようにし
たことにより、従来のものの上記の欠点を完全に
除去出来ない迄も、吐出ガスを利用したものに較
べて、無駄な圧縮仕事の減少はかつて効率を向上
せしめることができる冷凍装置の油戻し装置を提
供することを目的とするものである。 However, in conventional systems with this type of structure, the refrigerant gas that has been pressurized to the discharge pressure by the screw compressor is returned to the suction side for suction, which increases wasteful compression work that is useless for the refrigeration cycle. The defects that led to a decline in efficiency were corrected. The present invention cools the refrigerant liquid entering the evaporator with an economizer, takes out a part of the intermediate pressure refrigerant gas after evaporation, and guides it to the suction side of the compressor via the ejector. By suctioning the oil-containing refrigerant liquid and returning it to the rotor working space, it is less wasteful than a system that uses discharged gas, although the above-mentioned drawbacks of conventional systems cannot be completely eliminated. The reduction in compression work was previously aimed at providing an oil return device for a refrigeration system that could improve efficiency.
第2図は本発明の第1の実施態様を示し、冷媒
はスクリユー圧縮機1で圧縮され、吐出管31で
油分離機11にゆく。そこで分離された油は油ポ
ンプ12でひかれて油管34で油冷却器13にゆ
き、油管35によつて、スクリユー圧縮機の軸受
給油孔3にゆき、又並列に設けられた油管36に
よつて油噴射孔2にゆく。 FIG. 2 shows a first embodiment of the invention, in which the refrigerant is compressed in a screw compressor 1 and goes to an oil separator 11 through a discharge pipe 31. The separated oil is pumped by the oil pump 12, goes to the oil cooler 13 through the oil pipe 34, goes to the bearing oil supply hole 3 of the screw compressor through the oil pipe 35, and goes through the oil pipe 36 installed in parallel. Go to oil injection hole 2.
油分離機で油を分離した後、冷媒ガスは吐出管
32によつて凝縮器15にゆき、凝縮された冷媒
液は熱交換器18を経て配管43によつてエコノ
マイザー61にゆき、コンデンサーフロート62
を経て開口63でエコノマイザーフロート室64
に入り、エコノマイザーフロート65を経て配管
44で蒸発器17にゆき、ここで蒸発する。冷媒
ガスは吸入管50によつてスクリユー圧縮機1の
吸入孔51に戻る。エコノマイザーフロート室の
上部の気相部には分岐官46が設けられ、ガスは
そこからバイパス用の配管47、電磁弁66、温
度式自動膨張弁16、エゼクタ14、バイパス用
の配管48を経て、合流点49で吸入管50に合
流する。この温度式自動膨張弁16は感温筒60
によつて検知された温度によつて制御される。 After separating the oil in the oil separator, the refrigerant gas goes to the condenser 15 through the discharge pipe 32, and the condensed refrigerant liquid goes through the heat exchanger 18, goes through the pipe 43 to the economizer 61, and then passes through the condenser float. 62
through the opening 63 to the economizer float chamber 64
The water enters the tank, passes through the economizer float 65, goes to the evaporator 17 via piping 44, and is evaporated there. The refrigerant gas returns to the suction hole 51 of the screw compressor 1 through the suction pipe 50. A branch 46 is provided in the upper gas phase part of the economizer float chamber, and the gas passes from there through a bypass pipe 47, a solenoid valve 66, a thermostatic automatic expansion valve 16, an ejector 14, and a bypass pipe 48. , joins the suction pipe 50 at a junction 49 . This temperature-type automatic expansion valve 16 has a temperature-sensitive cylinder 60
controlled by the temperature sensed by the
蒸発器における油を多く含んだ冷媒液保有部は
油戻し管37によつて、熱交換器18を経てエゼ
クタ14の吸入部38と連結されている。又エコ
ノマイザーフロート室64は背圧調整弁71を有
する中間吸入管70によつてスクリユー圧縮機1
の中間吸入開孔72と連絡され、その背圧が調整
される。 The oil-rich refrigerant holding portion of the evaporator is connected to the suction portion 38 of the ejector 14 via the heat exchanger 18 by an oil return pipe 37. The economizer float chamber 64 is connected to the screw compressor 1 by an intermediate suction pipe 70 having a back pressure regulating valve 71.
The back pressure thereof is regulated.
第3図は別な実施態様を示し、エコノマイザー
61の形式が第2図の場合と相異するが、第2図
と同じ符号は同じ部品を示している。 FIG. 3 shows another embodiment in which the type of economizer 61 is different from that in FIG. 2, but the same reference numerals as in FIG. 2 indicate the same parts.
第3図において、凝縮器15を出た冷媒液は、
出口管33から配管43で密閉エコノマイザー6
1に入り、一部は並列して分岐した配管43′か
ら温度式自動膨張弁16を経てエコノマイザー6
1に入つてフラツシユし、配管43から来た冷媒
液を過冷却する。 In FIG. 3, the refrigerant liquid leaving the condenser 15 is
The economizer 6 is sealed from the outlet pipe 33 to the piping 43.
1, some of which are branched in parallel from piping 43' to economizer 6 via thermostatic automatic expansion valve 16.
1 and flashes, supercooling the refrigerant liquid coming from the pipe 43.
過冷却された冷媒液は熱交換器18を経て蒸発
器17に入る。75は冷媒流量調節弁、76は液
位調節器である。エコノマイザー61の気相部は
中間吸入管70より分岐し、配管47、電磁弁6
6、温度式自動膨張弁16、エゼクタ38に連結
される、更に、バイパス用の配管48によつて、
蒸発器17からの冷媒ガス吸入管50と合流点4
9で合流し、吸入開孔51でスクリユー圧縮機に
戻る。又エコノマイザーの気相部は背圧調整弁7
1を有する中間吸入管70によつて、スクリユー
圧縮機1の中間吸入開口72より圧縮機に吸入さ
れる、尚この時エコノマイザー圧は前記背圧調整
弁によつて、一定圧に保たれる。蒸発器17から
油を含む冷媒液は配管37で熱交換器18を経て
エゼクタ14の吸入点38に至ることは第2図の
場合と同様である。 The supercooled refrigerant liquid passes through the heat exchanger 18 and enters the evaporator 17 . 75 is a refrigerant flow control valve, and 76 is a liquid level regulator. The gas phase part of the economizer 61 branches from the intermediate suction pipe 70, and is connected to the pipe 47 and the solenoid valve 6.
6. The thermostatic automatic expansion valve 16 is connected to the ejector 38, and is further connected to the bypass pipe 48,
Refrigerant gas suction pipe 50 from evaporator 17 and confluence point 4
9 and return to the screw compressor at the suction opening 51. Also, the gas phase part of the economizer is equipped with a back pressure regulating valve 7.
1, the compressor is sucked into the compressor through the intermediate suction opening 72 of the screw compressor 1. At this time, the economizer pressure is maintained at a constant pressure by the back pressure regulating valve. . As in the case of FIG. 2, the refrigerant liquid containing oil from the evaporator 17 passes through the heat exchanger 18 through the pipe 37 and reaches the suction point 38 of the ejector 14.
上記の実施例は上述の如く構成されているの
で、次の如き顕著な効果を有する。 Since the above embodiment is constructed as described above, it has the following remarkable effects.
1 エコノマイザサイクルにおけるエコノマイザ
にて、蒸発器に入る冷媒液を冷却し(冷凍効果
を増大させる)蒸発した中間圧ガスを利用して
エゼクタを作用させる為吐出ガスを利用したも
のに較べて無駄な圧縮仕事の減少をはかれる。1 The economizer in the economizer cycle cools the refrigerant liquid entering the evaporator (increasing the refrigeration effect), and uses the evaporated intermediate pressure gas to actuate the ejector, which results in unnecessary compression compared to systems that use discharged gas. Work will be reduced.
2 油戻し管の途中に熱交換器を設けて冷凍装置
の低圧部分の油を含んだ冷媒と低圧部分に流入
する前の高圧冷媒液とを熱交換し前記高圧冷媒
液を過冷却して冷凍効果を増大し冷凍機の成績
係数を増大させる。2. A heat exchanger is installed in the middle of the oil return pipe to exchange heat between the oil-containing refrigerant in the low-pressure part of the refrigeration system and the high-pressure refrigerant liquid before flowing into the low-pressure part, thereby subcooling the high-pressure refrigerant liquid and freezing it. Increase effectiveness and increase coefficient of performance of refrigerator.
なお、圧縮機としては、スクリユー圧縮機以外
にもロータリーベーン式、ロータリーピストン
式、ルーツ式などの容積型圧縮機を用いてもよ
い。又、油噴射式でないものにも、軸受油回収な
どのために用いてもよい。 In addition, as the compressor, in addition to the screw compressor, a positive displacement compressor such as a rotary vane type, rotary piston type, or Roots type may be used. In addition, even non-oil injection type devices may be used for collecting oil from bearings, etc.
本発明は、圧縮機、凝縮器、エコノマイザー、
蒸発器並びにこれらを接続する冷媒経路により冷
凍サイクルを形成する冷凍装置の、エコノマイザ
又は中間吸入ラインの気相部の一部に分岐点を設
けてバイパス経路を分岐せしめ、該バイパス経路
の他端は前記圧縮機の吸入側に接続され、前記バ
イパス経路の途中にエゼクタを挿入し、該エゼク
タの吸入部と前記冷凍装置の低圧系統中における
油を含んだ冷媒液保有部とを油戻し経路にて連絡
したことにより、無駄な圧縮仕事を減少せしめて
効率を向上せしめることができる冷凍装置の油戻
し装置を提供することができ、実用上極めて大な
る効果を有するものである。 The present invention includes compressors, condensers, economizers,
In a refrigeration system that forms a refrigeration cycle by an evaporator and a refrigerant path connecting these, a branch point is provided in a part of the gas phase part of the economizer or intermediate suction line to branch a bypass path, and the other end of the bypass path is An ejector is connected to the suction side of the compressor and inserted in the middle of the bypass path, and the suction part of the ejector and the refrigerant liquid holding part containing oil in the low pressure system of the refrigeration system are connected through an oil return path. As a result of this communication, it is possible to provide an oil return device for a refrigeration system that can reduce wasteful compression work and improve efficiency, which has an extremely large practical effect.
第1図は冷凍装置の従来例のフローシート、第
2図は本発明の実施例のフローシート、第3図は
別な実施態様のフローシートを夫々示す。
符号の説明、1……スクリユー圧縮機、2……
油噴射孔、3……軸受給油孔、11……油分離、
12……油ポンプ、13……油冷却器、14……
エゼクタ、15……凝縮器、16……温度式自動
膨張弁、17……蒸発器、18……熱交換器、3
1,32,33……吐出管、34,35,36…
…油管、37……油戻し管、38……エゼクタ吸
入部、43,47……配管、48……バイパス用
配管、60……感温筒、61……エコノマイザ
ー、62……コンデンサーフロート、63……開
口、64……エコノマイザーフロート室、65…
…エコノマイザーフロート、66……電磁弁、7
0……中間吸入管、71……背圧調整弁、72…
…吸入開口。
FIG. 1 shows a flow sheet of a conventional example of a refrigeration system, FIG. 2 shows a flow sheet of an embodiment of the present invention, and FIG. 3 shows a flow sheet of another embodiment. Explanation of symbols, 1... Screw compressor, 2...
Oil injection hole, 3... bearing oil supply hole, 11... oil separation,
12...Oil pump, 13...Oil cooler, 14...
Ejector, 15... Condenser, 16... Temperature type automatic expansion valve, 17... Evaporator, 18... Heat exchanger, 3
1, 32, 33...discharge pipe, 34, 35, 36...
... Oil pipe, 37 ... Oil return pipe, 38 ... Ejector suction section, 43, 47 ... Piping, 48 ... Bypass pipe, 60 ... Temperature sensing cylinder, 61 ... Economizer, 62 ... Condenser float, 63...Opening, 64...Economizer float chamber, 65...
...Economizer float, 66...Solenoid valve, 7
0... Intermediate suction pipe, 71... Back pressure regulating valve, 72...
...Inhalation opening.
Claims (1)
にこれらを接続する冷媒経路により冷凍サイクル
を形成する冷凍装置において、エコノマイザーの
気相部の一部に分岐点を設け、そこからバイパス
配管よりなるバイパス経路を分岐せしめ、該バイ
パス経路の他端は前記圧縮機の吸入側に接続さ
れ、前記のバイパス経路の途中にエゼクタを挿入
し、該エゼクタの吸入部と前記蒸発器中の油を含
んだ冷媒液保有部とを、油戻し管にて連絡したこ
とを特徴とする冷凍装置の油戻し装置。 2 前記のバイパス経路において、前記の分岐点
と前記のエゼクタの間に温度式自動膨張弁を備
え、さらに前記のバイパス経路中のエゼクタと圧
縮機の吸入側との間のバイパス配管か、又は圧縮
機の吐出配管に温度を検出する温度検出器を備
え、該温度検出器の信号により、前記の温度式自
動膨張弁の開度を制御する制御機構を備えている
ことを特徴とする前記特許請求の範囲第1項記載
の油戻し装置。 3 前記の蒸発器内の冷媒液保有部と前記エゼク
タの吸入部とを連絡する前記油戻し管の途中に熱
交換器を設け、該熱交換器においては前記油戻し
管を通過する油を含んだ冷媒液と、高圧側からの
冷媒液とを熱交換するよう構成されたことを特徴
とする前記特許請求の範囲第1項記載の油戻し装
置。[Claims] 1. In a refrigeration system in which a refrigeration cycle is formed by a compressor, a condenser, an economizer, an evaporator, and a refrigerant path connecting these, a branch point is provided in a part of the gas phase part of the economizer, and A bypass path consisting of bypass piping is branched from the bypass path, the other end of the bypass path is connected to the suction side of the compressor, and an ejector is inserted in the middle of the bypass path, and the suction section of the ejector and the inside of the evaporator are connected to each other. An oil return device for a refrigeration system, characterized in that the oil return device is connected to a refrigerant liquid holding portion containing oil through an oil return pipe. 2 In the bypass route, a thermostatic automatic expansion valve is provided between the branch point and the ejector, and a bypass piping or compressor is provided between the ejector in the bypass route and the suction side of the compressor. The above patent claim is characterized in that the discharge pipe of the machine is equipped with a temperature detector that detects the temperature, and a control mechanism that controls the opening degree of the temperature-type automatic expansion valve based on a signal from the temperature detector. The oil return device according to item 1. 3. A heat exchanger is provided in the middle of the oil return pipe that connects the refrigerant liquid holding part in the evaporator and the suction part of the ejector, and the heat exchanger contains oil passing through the oil return pipe. 2. The oil return device according to claim 1, wherein the oil return device is configured to exchange heat between the refrigerant liquid from the high pressure side and the refrigerant liquid from the high pressure side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19551981A JPS5896955A (en) | 1981-12-04 | 1981-12-04 | Oil return device for refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19551981A JPS5896955A (en) | 1981-12-04 | 1981-12-04 | Oil return device for refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5896955A JPS5896955A (en) | 1983-06-09 |
| JPH0120697B2 true JPH0120697B2 (en) | 1989-04-18 |
Family
ID=16342429
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19551981A Granted JPS5896955A (en) | 1981-12-04 | 1981-12-04 | Oil return device for refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5896955A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104075475A (en) * | 2013-03-26 | 2014-10-01 | 荏原冷热系统株式会社 | Turbine refrigerator |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9200820B2 (en) | 2009-10-20 | 2015-12-01 | Mitsubishi Electric Corporation | Heat pump apparatus with ejector cycle |
| JP2015190662A (en) * | 2014-03-27 | 2015-11-02 | 荏原冷熱システム株式会社 | turbo refrigerator |
| JP2015194300A (en) * | 2014-03-31 | 2015-11-05 | 荏原冷熱システム株式会社 | turbo refrigerator |
| JP6782013B2 (en) * | 2017-02-03 | 2020-11-11 | 宏和工業株式会社 | Cooling unit |
-
1981
- 1981-12-04 JP JP19551981A patent/JPS5896955A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104075475A (en) * | 2013-03-26 | 2014-10-01 | 荏原冷热系统株式会社 | Turbine refrigerator |
| JP2014190579A (en) * | 2013-03-26 | 2014-10-06 | Ebara Refrigeration Equipment & Systems Co Ltd | Turbo freezer |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5896955A (en) | 1983-06-09 |
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