JPH0428962A - Oil purifying device for freezer device - Google Patents
Oil purifying device for freezer deviceInfo
- Publication number
- JPH0428962A JPH0428962A JP13284590A JP13284590A JPH0428962A JP H0428962 A JPH0428962 A JP H0428962A JP 13284590 A JP13284590 A JP 13284590A JP 13284590 A JP13284590 A JP 13284590A JP H0428962 A JPH0428962 A JP H0428962A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- oil
- heater
- evaporator
- refrigerant heater
- 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
- 239000003507 refrigerant Substances 0.000 claims abstract description 86
- 238000005057 refrigeration Methods 0.000 claims description 20
- 238000007670 refining Methods 0.000 claims description 11
- 238000005192 partition Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 4
- 238000005187 foaming Methods 0.000 abstract 2
- 238000010586 diagram Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は圧縮機を用いた冷凍装置において蒸発器内の
冷媒に混入した油を抽出する装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a device for extracting oil mixed in refrigerant in an evaporator in a refrigeration system using a compressor.
第3図は従来の冷凍装置における油精製装置の一例を示
す冷凍サイクル図であり、図において、1は圧縮機、2
は凝縮器、3は膨脹弁、4は蒸発器、5は圧縮機1と凝
縮器2とを接続する吐出管、6は凝縮器2と膨脹弁3と
を接続する液出口管、7は膨脹弁3と蒸発器4とを接続
する液入口管、8は蒸発器4と圧縮機1とを接続する吸
入管で、これらにより冷凍機の冷凍サイクルが形成され
て−・る。9は蒸発器4の中の冷媒に混入した油を抽出
し、圧縮機1に戻すヒータ9aを有する冷媒加熱器で、
この冷媒加熱器9は接続管10を介して蒸発器4に接続
されている。11は冷媒加熱器9と吸入管8とを接続す
る接続管、12.13は冷媒加熱器9の底部と圧縮機1
とを油ポンプ14を介して接続する油戻し管である。FIG. 3 is a refrigeration cycle diagram showing an example of an oil refining device in a conventional refrigeration system. In the figure, 1 is a compressor, 2
is a condenser, 3 is an expansion valve, 4 is an evaporator, 5 is a discharge pipe that connects the compressor 1 and the condenser 2, 6 is a liquid outlet pipe that connects the condenser 2 and the expansion valve 3, and 7 is an expansion pipe. A liquid inlet pipe 8 connects the valve 3 and the evaporator 4, and a suction pipe 8 connects the evaporator 4 and the compressor 1, forming a refrigeration cycle of the refrigerator. 9 is a refrigerant heater having a heater 9a that extracts oil mixed in the refrigerant in the evaporator 4 and returns it to the compressor 1;
This refrigerant heater 9 is connected to the evaporator 4 via a connecting pipe 10. 11 is a connecting pipe that connects the refrigerant heater 9 and the suction pipe 8; 12.13 is the bottom of the refrigerant heater 9 and the compressor 1;
This is an oil return pipe that connects the two via the oil pump 14.
次に動作について説明する。Next, the operation will be explained.
まず、蒸発器4より油を含んだ冷媒を接続管10で冷媒
加熱器9に導いてヒータ9aにより加熱する。このため
、冷媒は蒸発して冷媒ガスを接続管11を通って吸入管
8に導く。このように冷媒を連続的に冷媒加熱器9に導
いて加熱することにより冷媒加熱器9の底部には常に濃
縮された油が溜まることになり、この濃縮された油は油
ポンプ14により油戻し管12.13を通って圧縮機1
へ戻ることになる。なお、従来例の関連技術としては例
えば特公平1−20697号公報がある。First, the refrigerant containing oil from the evaporator 4 is guided to the refrigerant heater 9 through the connecting pipe 10 and heated by the heater 9a. Therefore, the refrigerant evaporates and the refrigerant gas is guided to the suction pipe 8 through the connecting pipe 11. By continuously guiding the refrigerant to the refrigerant heater 9 and heating it in this way, concentrated oil always accumulates at the bottom of the refrigerant heater 9, and this concentrated oil is returned to the oil by the oil pump 14. Compressor 1 through pipe 12.13
will return to. In addition, as a related art of the conventional example, there is, for example, Japanese Patent Publication No. 1-20697.
従来の冷凍装置における油精製装置は以上のように構成
されているので、冷媒加熱器9には常に接続管10を介
して油を含んだ冷媒が流入する一方、ヒータ9aにより
冷媒は加熱されて冷媒ガスを発生させているために冷媒
加熱器9の底部に溜まる油の濃度はヒータ9aの容量の
関係で、所定の濃度でバランスしてしまい、油の濃度を
100チに近づけることはできないという問題点があっ
た。また、このようにある濃度でバランスしている状態
で冷凍機を停止し、再度起動させると、冷媒加熱器9中
の冷媒がフォーミングし、冷媒ガスと油とが同時に吸入
管8に吸込まれ、冷媒加熱器9中の油がなくなってしま
うという問題点があり、これを防止するために別に油タ
ンクやヒータ(図示しない)を設ける必要があるので、
装置が複雑でコスト高となってしまうという問題点があ
った。Since the oil refining device in the conventional refrigeration system is configured as described above, the refrigerant containing oil always flows into the refrigerant heater 9 via the connecting pipe 10, while the refrigerant is heated by the heater 9a. Because refrigerant gas is generated, the concentration of oil that accumulates at the bottom of the refrigerant heater 9 is balanced at a predetermined concentration due to the capacity of the heater 9a, and the oil concentration cannot be brought close to 100 g. There was a problem. Furthermore, when the refrigerator is stopped and restarted in a state where the concentration is balanced at a certain concentration, the refrigerant in the refrigerant heater 9 forms, and the refrigerant gas and oil are simultaneously sucked into the suction pipe 8. There is a problem that the oil in the refrigerant heater 9 runs out, and to prevent this, it is necessary to separately provide an oil tank and a heater (not shown).
There was a problem that the device was complicated and the cost was high.
この発明は上記のような問題点を解消するためになされ
たもので、連続的に100チ近(の油を精製できるよう
にし、冷凍機の起動時に冷媒加熱器の冷媒のフォーミン
グ現象をなくす冷凍装置における油精製装置を得ること
を目的とする。This invention was made to solve the above-mentioned problems, and it is a refrigeration system that makes it possible to continuously refine nearly 100 inches of oil and eliminates the forming phenomenon of the refrigerant in the refrigerant heater when starting the refrigerator. The purpose is to obtain an oil refining device in the device.
この発明に係る冷凍装置における油精製装置は圧縮機、
凝縮器、膨脹弁、蒸発器および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と共に、冷媒に混入し
た油を抽出する冷媒加熱器を上記冷凍サイクルとは異な
る経路で上記蒸発器と上記圧縮機との間に接続したもの
であって、堰を有する仕切板により形成され、上記蒸発
器より供給される油を含む冷媒が一時貯溜される上部室
および上記仕切板を貫通するヒータ入りの伝熱管よりな
る冷媒加熱器と、この冷媒加熱器に設けられ、冷媒加熱
器の底面に溜まった油の量を調整する油面調整器と、上
記蒸発器と上記冷媒加熱器との間に接続され、上記油面
調整器により開閉制御される電磁弁とを備えたものであ
る。The oil refining device in the refrigeration device according to the present invention includes a compressor,
A refrigeration cycle is formed by a condenser, an expansion valve, an evaporator, and a refrigerant path connecting these, and a refrigerant heater for extracting oil mixed in the refrigerant is connected to the evaporator and compressor through a route different from the refrigeration cycle. an upper chamber formed by a partition plate having a weir and in which the oil-containing refrigerant supplied from the evaporator is temporarily stored; and a heat transfer tube containing a heater that passes through the partition plate. a refrigerant heater consisting of; an oil level regulator provided in the refrigerant heater to adjust the amount of oil accumulated on the bottom surface of the refrigerant heater; connected between the evaporator and the refrigerant heater; It is equipped with a solenoid valve whose opening and closing are controlled by the oil level regulator.
この発明における油精製装置は蒸発器から冷媒加熱器の
上部室に油を含んだ冷媒を導き、油を含んだ冷媒を上部
室を貫通する伝熱管の上部から下部に沿わせて落下させ
る過程で冷媒ガスを蒸発させて油だけを底部に貯溜させ
るようにすると共に、上記蒸発器と冷媒加熱器とを接続
する接続管に設けた電磁弁を上記油面調整器により開閉
制御するようにしたもので、連続的に100%近くの油
を精製できるようにし、また冷凍機の起動時に冷媒加熱
器の冷媒のフォーミング現象を亡くせるようにしたもの
である。The oil refining device of the present invention introduces oil-containing refrigerant from the evaporator to the upper chamber of the refrigerant heater, and in the process of dropping the oil-containing refrigerant from the upper part to the lower part of the heat transfer tube that penetrates the upper chamber. The refrigerant gas is evaporated and only the oil is stored at the bottom, and the solenoid valve provided in the connecting pipe connecting the evaporator and the refrigerant heater is opened and closed by the oil level regulator. This allows for nearly 100% oil to be refined continuously, and also eliminates the forming phenomenon of the refrigerant in the refrigerant heater when starting up the refrigerator.
以下、この発明の一実施例を図について説明する。 An embodiment of the present invention will be described below with reference to the drawings.
第1図はこの発明の一実施例を示す冷凍サイクル図、第
2図は冷媒加熱器を示す縦断面図で、第1図において第
3図と同一または均等部分には同一符号を付して重複説
明を省略する。図において、15は接続管10により蒸
発器4に接続されて℃・る詳細を後述する冷媒加熱器、
16は冷媒加熱器15の底部に貯溜する油の量を調整す
る油面調整器、17は接続管10に設けられた電磁弁で
、この電磁弁17は油面調整器16よりの信号により開
閉する。FIG. 1 is a refrigeration cycle diagram showing an embodiment of the present invention, and FIG. 2 is a longitudinal sectional view showing a refrigerant heater. In FIG. 1, the same or equivalent parts as in FIG. Omit duplicate explanations. In the figure, 15 is a refrigerant heater connected to the evaporator 4 by a connecting pipe 10, the details of which will be described later.
16 is an oil level regulator that adjusts the amount of oil stored at the bottom of the refrigerant heater 15; 17 is a solenoid valve provided in the connecting pipe 10; this solenoid valve 17 is opened and closed by a signal from the oil level regulator 16; do.
しかして、1Bは冷媒加熱器15内に堰19aを有する
仕切板19によって形成された上部室で、この上部室1
8は接続管10より導かれる油を含んだ冷媒を一時的に
貯える。20は仕切板19の中心部を貫通する伝熱管で
、この伝熱管20にはスパイラルフィン20aが施され
、伝熱管20内にはヒータ9aが挿入されている。1B is an upper chamber formed by a partition plate 19 having a weir 19a in the refrigerant heater 15;
8 temporarily stores the oil-containing refrigerant introduced from the connecting pipe 10. Reference numeral 20 denotes a heat exchanger tube that passes through the center of the partition plate 19. This heat exchanger tube 20 is provided with spiral fins 20a, and a heater 9a is inserted into the heat exchanger tube 20.
次に動作について説明する。Next, the operation will be explained.
圧縮機1、吐出管5、凝縮器2、液出口管6、膨脹弁3
、液入口管7、蒸発器4および吸入管8を通る冷凍サイ
クルと、接続管10.11を通る冷媒の流れおよび油戻
し管12.13を通って圧縮機1に返戻される油の流れ
は従来例と同様であるので、その説明は省略する。Compressor 1, discharge pipe 5, condenser 2, liquid outlet pipe 6, expansion valve 3
, the refrigeration cycle through liquid inlet pipe 7, evaporator 4 and suction pipe 8, the flow of refrigerant through connecting pipe 10.11 and the flow of oil returned to compressor 1 through oil return pipe 12.13. Since this is the same as the conventional example, its explanation will be omitted.
蒸発器4から取出した油を含んだ冷媒は電磁弁17およ
び接続管10を通って冷媒加熱器15の上部室18に流
入する。この冷媒は堰19aをオーバーフロースルまで
溜まり、オーバーフローした冷媒は堰19aと伝熱管2
0との隙間を通って落下する。この落下した冷媒は伝熱
管20に施されたスパイラルフィン20aを伝って徐々
に落下する過程でヒータ9aにより加熱され、伝熱管2
0の下部に到達する間に冷媒だけが蒸発する。そして、
蒸発した冷媒ガスは接続管11を通って圧縮機1の低圧
側に逃がされ、濃縮された油は冷媒加熱器15の底部に
滴下される。しかるのち、伝熱管20の下部から滴下し
た油が冷媒加熱器15の底部に必要以上に溜まると、油
面調整器16がこれを検知して電磁弁17に信号を発信
して電磁弁17を閉じ、冷媒の流入を遮断する。そして
、油は油ポンプ14により圧縮機1へ送出されるが、油
面が低下すると、油面調整器16の信号で電磁弁17は
開き、再び油が冷媒加熱器15に供給されて精製される
ことになる。The oil-containing refrigerant taken out from the evaporator 4 passes through the solenoid valve 17 and the connecting pipe 10 and flows into the upper chamber 18 of the refrigerant heater 15 . This refrigerant accumulates until it overflows the weir 19a, and the overflowed refrigerant passes through the weir 19a and the heat exchanger tube 2.
It falls through the gap with 0. This fallen refrigerant is heated by the heater 9a in the process of gradually falling along the spiral fins 20a provided on the heat exchanger tube 20, and is heated by the heater 9a.
Only the refrigerant evaporates while reaching the bottom of 0. and,
The evaporated refrigerant gas is allowed to escape through the connecting pipe 11 to the low pressure side of the compressor 1, and the concentrated oil is dripped into the bottom of the refrigerant heater 15. Afterwards, when the oil dripping from the lower part of the heat transfer tube 20 accumulates at the bottom of the refrigerant heater 15 more than necessary, the oil level regulator 16 detects this and sends a signal to the solenoid valve 17 to turn the solenoid valve 17 on. Close to cut off the inflow of refrigerant. The oil is sent to the compressor 1 by the oil pump 14, but when the oil level drops, the solenoid valve 17 is opened by a signal from the oil level regulator 16, and the oil is again supplied to the refrigerant heater 15 and purified. That will happen.
なお、上記実施例では伝熱管を1本として説明したが、
油の精製の必要量に応じて伝熱管およびヒータの本数は
適宜選択できるものである。In addition, in the above embodiment, the explanation was made using one heat exchanger tube, but
The number of heat exchanger tubes and heaters can be selected as appropriate depending on the amount of oil required for refining.
以上のようにこの発明によれば冷凍装置における油精製
装置を蒸発器から冷媒加熱器の上部室に油を含んだ冷媒
を導き、油を含んだ冷媒を上部室を貫通する伝熱管の上
部から下部に沿わせて落下させる過程で冷媒ガスを蒸発
させて油だけを底部に貯溜させるようにすると共に、上
記蒸発器と冷媒加熱器とを接続する接続管に設けた電磁
弁を上記油面調整器により開閉制御するように構成した
ので、連続的に100%近くの油を精製できるようにし
、また冷凍機の起動時に冷媒加熱器の冷媒のフォーミン
グ現象をなくせるという効果がある。As described above, according to the present invention, an oil refining device in a refrigeration system is used to guide oil-containing refrigerant from an evaporator to an upper chamber of a refrigerant heater, and to direct oil-containing refrigerant from the upper part of a heat transfer tube passing through the upper chamber. In the process of falling along the bottom, the refrigerant gas is evaporated so that only the oil is stored at the bottom, and a solenoid valve installed in the connecting pipe connecting the evaporator and the refrigerant heater is used to adjust the oil level. Since the system is configured to open and close by controlling the opening and closing of the refrigerant, it is possible to continuously refine nearly 100% of the oil, and it is also effective in eliminating the forming phenomenon of the refrigerant in the refrigerant heater when starting up the refrigerator.
第1図はこの発明の一実施例による冷凍装置における油
精製装置を示す冷凍サイクル図、第2図は冷媒加熱器を
示す縦断面図、第3図は従来の冷凍装置における油精製
装置の一例を示す冷凍サイクル図である。
1・・・圧縮機、2・・・凝縮器、3・・・膨脹弁、4
・・・蒸発器、15・・・冷媒加熱器、16・・・油面
調整器、17・・・電磁弁、18・・・上部室、19・
・・仕切板、19a・・・堰、20・・・伝熱管。
なお、図中、同一符号は同一または相当部分を示す0
特許出願人 三菱電機株式会社(外2名)
第
図Fig. 1 is a refrigeration cycle diagram showing an oil refining device in a refrigeration system according to an embodiment of the present invention, Fig. 2 is a longitudinal sectional view showing a refrigerant heater, and Fig. 3 is an example of an oil refining device in a conventional refrigeration system. It is a refrigeration cycle diagram showing. 1... Compressor, 2... Condenser, 3... Expansion valve, 4
... Evaporator, 15... Refrigerant heater, 16... Oil level regulator, 17... Solenoid valve, 18... Upper chamber, 19...
... Partition plate, 19a... Weir, 20... Heat exchanger tube. In addition, in the figures, the same reference numerals indicate the same or corresponding parts.
Patent applicant: Mitsubishi Electric Corporation (2 others) Figure
Claims (1)
る冷媒経路により冷凍サイクルを形成すると共に、冷媒
に混入した油を抽出する冷媒加熱器を上記冷凍サイクル
とは異なる経路で上記蒸発器と上記圧縮機との間に接続
した冷凍装置における油精製装置において、堰を有する
仕切板により形成され、上記蒸発器より供給される油を
含む冷媒が一時貯溜される上部室および上記仕切板を貫
通するヒータ入りの伝熱管よりなる冷媒加熱器と、この
冷媒加熱器に設けられ、冷媒加熱器の底面に溜まった油
の量を調整する油面調整器と、上記蒸発器と上記冷媒加
熱器との間に接続され、上記油面調整器により開閉制御
される電磁弁とを備えたことを特徴とする冷凍装置にお
ける油精製装置。A refrigeration cycle is formed by a compressor, a condenser, an expansion valve, an evaporator, and a refrigerant path connecting these, and a refrigerant heater for extracting oil mixed in the refrigerant is connected to the evaporator through a path different from the refrigeration cycle. In an oil refining device in a refrigeration system connected between the compressor, the upper chamber is formed by a partition plate having a weir and passes through the partition plate and an upper chamber in which a refrigerant containing oil supplied from the evaporator is temporarily stored. a refrigerant heater made of a heat transfer tube containing a heater; an oil level regulator provided in the refrigerant heater to adjust the amount of oil accumulated on the bottom of the refrigerant heater; the evaporator and the refrigerant heater; An oil refining device for a refrigeration system, comprising: a solenoid valve connected between the oil level controller and the solenoid valve, the opening and closing of which is controlled by the oil level regulator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13284590A JPH0428962A (en) | 1990-05-23 | 1990-05-23 | Oil purifying device for freezer device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13284590A JPH0428962A (en) | 1990-05-23 | 1990-05-23 | Oil purifying device for freezer device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0428962A true JPH0428962A (en) | 1992-01-31 |
Family
ID=15090863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13284590A Pending JPH0428962A (en) | 1990-05-23 | 1990-05-23 | Oil purifying device for freezer device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0428962A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008249230A (en) * | 2007-03-30 | 2008-10-16 | Yanmar Co Ltd | Air conditioner |
CN117469822A (en) * | 2023-12-27 | 2024-01-30 | 珠海格力电器股份有限公司 | Air conditioning unit, control method and storage medium |
-
1990
- 1990-05-23 JP JP13284590A patent/JPH0428962A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008249230A (en) * | 2007-03-30 | 2008-10-16 | Yanmar Co Ltd | Air conditioner |
CN117469822A (en) * | 2023-12-27 | 2024-01-30 | 珠海格力电器股份有限公司 | Air conditioning unit, control method and storage medium |
CN117469822B (en) * | 2023-12-27 | 2024-03-19 | 珠海格力电器股份有限公司 | Air conditioning unit, control method and storage medium |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2417344C2 (en) | Device and procedure for control of cooling systems | |
KR100609845B1 (en) | Chiller for semiconductor process apparatus | |
US5032157A (en) | Icemaker system with wide range condensing temperatures | |
CN105371532A (en) | Air conditioner | |
AR000280A1 (en) | A method and apparatus for separating a substance from a liquid mixture by fractional crystallization | |
KR20010074933A (en) | Absorption refrigeration machine | |
JPH0428962A (en) | Oil purifying device for freezer device | |
JPH01169278A (en) | Bypass for liquid and gas | |
US3167928A (en) | Method of and apparatus for venting fixed gas from absorption refrigeration system | |
US2112537A (en) | Refrigeration | |
US1866992A (en) | Refrigeration | |
US2195387A (en) | Automatic level control | |
US5782099A (en) | Method for controlling an absorption system | |
JPH0447224B2 (en) | ||
US2721455A (en) | Absorption refrigeration | |
US1779409A (en) | Refrigerating apparatus | |
US2093839A (en) | Refrigerating apparatus | |
US6629421B1 (en) | Method of and an apparatus for a self-governing pulse feeding refrigerant | |
US1943616A (en) | Refrigeration apparatus | |
JPH05322330A (en) | Freezer device | |
US1884186A (en) | Refrigeration | |
CN116857799A (en) | Multi-split heat pump air conditioner and flash tank liquid level control method thereof | |
US3259182A (en) | Apparatus for the removal of fixed gas from absorption refrigeration process | |
JPH01247969A (en) | Air-cooled absorption refrigerator | |
US1983766A (en) | Refrigerating apparatus |