JPH0368407A - Oil purifier - Google Patents

Oil purifier

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Publication number
JPH0368407A
JPH0368407A JP1203514A JP20351489A JPH0368407A JP H0368407 A JPH0368407 A JP H0368407A JP 1203514 A JP1203514 A JP 1203514A JP 20351489 A JP20351489 A JP 20351489A JP H0368407 A JPH0368407 A JP H0368407A
Authority
JP
Japan
Prior art keywords
oil
filter
centrifugal
chamber
pump chamber
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.)
Granted
Application number
JP1203514A
Other languages
Japanese (ja)
Other versions
JP2886190B2 (en
Inventor
Hiroshi Matsumoto
弘 松本
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.)
HANSHIN NAINENKI KOGYO KK
Original Assignee
HANSHIN NAINENKI KOGYO KK
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 HANSHIN NAINENKI KOGYO KK filed Critical HANSHIN NAINENKI KOGYO KK
Priority to JP1203514A priority Critical patent/JP2886190B2/en
Publication of JPH0368407A publication Critical patent/JPH0368407A/en
Application granted granted Critical
Publication of JP2886190B2 publication Critical patent/JP2886190B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Filtration Of Liquid (AREA)
  • Centrifugal Separators (AREA)

Abstract

PURPOSE:To reduce the running cost of the oil purifier by providing a centrifugal separator and a filter and using the centrifugal force produced from the separator also for pumping. CONSTITUTION:When untreated oil is introduced, a centrifugal separation chamber 13 and a pump room 14 are rotated, and the centrifugal force is exerted on the introduced oil. The coarse contaminants are separated from oil by the centrifugal force in the chamber 13. Oil is successively introduced into the chamber 13, hence the oil level is raised, and the centrifugally separated oil is sent into the room 14 through an opening 14b. The oil introduced into the room 14 is subject to strong centrifugal force, and the pressure is progressively increased toward the outside. The oil in the room 14 is forced into an oil pipe 40 by the high pressure and conveyed to the filter 4. Consequently, the fine contaminants are filtered off, and the oil is purified.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は例えばディーゼルエンジン用の潤滑油の清浄化
に用いることができる油清浄装置に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an oil cleaning device that can be used, for example, to clean lubricating oil for a diesel engine.

〈従来の技術〉 第3図に従来の油清浄装置の構成図を示す、1は遠心分
離機、2は油タンク、3は輸送ポンプ、4は濾過機であ
る。使用ずみの油が油入口から遠心分離機1に入れられ
、遠心分離力によって粗混入物が油から除去される。遠
心分離された油は一旦油タンク2に収容され、さらに輸
送ポンプ3で汲み上げられて濾過機4に送られ、そこで
残留の微細混入物が濾過される。
<Prior Art> Fig. 3 shows a configuration diagram of a conventional oil purifying device, in which 1 is a centrifugal separator, 2 is an oil tank, 3 is a transport pump, and 4 is a filter. Used oil is introduced into the centrifuge 1 through the oil inlet, and coarse contaminants are removed from the oil by centrifugal force. The centrifuged oil is temporarily stored in an oil tank 2, then pumped up by a transport pump 3 and sent to a filter 4, where the remaining fine contaminants are filtered out.

〈発明が解決しようとする課題〉 ところが上記従来の装置では、遠心分離機を経た油が一
旦油タンク2に溜められ、さらに別に設けた輸送ポンプ
3で濾過機4に送られる構成となっているため、前記輸
送ポンプ3とそれを駆動するモータが必要となり、ラン
ニングコスト等が高くなる欠点があった。また油タンク
2も別に設けなければならない等の欠点があった。
<Problems to be Solved by the Invention> However, in the conventional apparatus described above, the oil that has passed through the centrifuge is temporarily stored in the oil tank 2, and is further sent to the filter 4 by a separately provided transport pump 3. Therefore, the transport pump 3 and a motor for driving it are required, which has the drawback of increasing running costs. Further, there was a drawback that the oil tank 2 had to be provided separately.

そこで本発明は上記従来装置の欠点を解消し、省エネ、
省スペースを図ることができ、また使用部材を少なくし
て簡潔な構成とすることができる油清浄装置の提供を目
的とする。
Therefore, the present invention eliminates the drawbacks of the above conventional devices, saves energy,
An object of the present invention is to provide an oil cleaning device that can save space and has a simple configuration by reducing the number of members used.

〈課題を解決するための手段〉 上記目的を達成するため、本発明の油清浄装置は、油中
の粗混入物を遠心分離する遠心分離機と、輸送されてく
る遠心分離後の油から微細混入物を濾過する濾過機とを
少なくとも有し、前記遠心分離機で発生する遠心力をポ
ンプ作用に兼用して遠心分離後の油を前記濾過機に送る
よう構成したことを第1の特徴としている。
<Means for Solving the Problems> In order to achieve the above object, the oil cleaning device of the present invention includes a centrifugal separator that centrifugally separates coarse contaminants in oil, and a centrifugal separator that centrifuges coarse contaminants in oil, and fine particles from centrifuged oil that is being transported. The first feature is that the oil is configured to include at least a filter for filtering contaminants, and the centrifugal force generated by the centrifugal separator is also used as a pumping action to send the centrifuged oil to the filter. There is.

また本発明の油清浄装置は、上記第1の特徴に加えて、
遠心分離後の油を濾過機へ送るためのポンプ室と遠心分
離室とを同一回転軸上に別室にして設けたことを第2の
特徴としている。
Moreover, in addition to the above first feature, the oil cleaning device of the present invention has the following features:
The second feature is that a pump chamber for sending centrifuged oil to a filter and a centrifugal separation chamber are provided as separate chambers on the same rotating shaft.

また本発明の油清浄装置は、上記第2の特徴に加えて、
ポンプ室上部は開放されており、オーバーフロー油の回
収手段が設けられていることを第3の特徴としている。
In addition to the second feature, the oil purifying device of the present invention also has the following features:
The third feature is that the upper part of the pump chamber is open and a means for collecting overflow oil is provided.

く作用〉 上記第1の特徴によれば、遠心分離機で発生する遠心力
がポンプ作用に兼用されることにより、遠心分離後の油
を濾過機へ輸送するための特別のポンプを不要とするこ
とができる。また遠心分離後の油を直接的に濾過機へ送
ることが可能となるので、遠心分離後の油を一旦溜める
ためのタンク等を不要とすることができる。
According to the first feature, the centrifugal force generated by the centrifuge is used for pumping action, thereby eliminating the need for a special pump to transport the centrifuged oil to the filter. be able to. Further, since the oil after centrifugation can be sent directly to the filter, it is possible to eliminate the need for a tank or the like to temporarily store the oil after centrifugation.

また上記第2の特徴によれば、遠心分離室とポンプ室と
が同一回転軸上ではあるが別室にして設けられているの
で、ポンプ動作に必要な部材等により遠心分離室におけ
る分離効果に悪影響を及ぼすことが生じない。もし、遠
心分離室が同時にポンプ室でもある場合、ポンプ動作に
必要な部材が遠心分離されようとする油を掻き混ぜるこ
とになり、遠心分離作用を低下させる。勿論遠心分離室
とポンプ室とが同一回転軸上にあるということは、遠心
分離用のモータによる遠心力をごく簡単にポンプ室にも
及ばしめることができるわけで、装置の構成が非常に簡
単になる。
Furthermore, according to the second feature, the centrifugal separation chamber and the pump chamber are located on the same rotation axis but are separate rooms, so the separation effect in the centrifugal separation chamber is adversely affected by the components necessary for pump operation. This will not cause any adverse effects. If the centrifugation chamber also serves as a pump chamber, the components necessary for the pump operation will agitate the oil to be centrifuged, reducing the centrifugal action. Of course, the fact that the centrifugal separation chamber and the pump chamber are on the same rotational axis means that the centrifugal force from the centrifugal motor can be easily applied to the pump chamber, making the configuration of the device extremely simple. become.

また上記第3の特徴によれば、ポンプ室上部が開放され
ることにより、輸送先の濾過機に目詰まりを起こしたよ
うな場合には、ポンプ室内に油が満ちて、やがて油がオ
ーバーフローする。がポンプ室からの吐出圧力は一定に
保たれるため、圧力調整弁等を必要としない。またオー
バーフローの有無及び程度により濾過機の濾材の詰まり
具合及び洗浄或いは取り替え時期を知ることができる。
Furthermore, according to the third feature, by opening the upper part of the pump chamber, if the filter at the destination is clogged, the pump chamber will be filled with oil and the oil will eventually overflow. . However, the discharge pressure from the pump chamber is kept constant, so there is no need for a pressure regulating valve. Furthermore, it is possible to know the degree of clogging of the filter medium of the filter and the timing of cleaning or replacement based on the presence or absence and degree of overflow.

勿論オーバーフロー油は回収手段により回収されて、再
利用に供される。
Of course, the overflow oil is recovered by the recovery means and provided for reuse.

〈実施例〉 第1図は本発明実施例の全体構成図、第2図は要部の断
面図である。遠心分離機10に対して未処理油の導入管
20が設けられており、遠心分離機10からはオーバー
フロー油の回収管30と濾過機4への油輸送管40が設
けられている。
<Embodiment> FIG. 1 is an overall configuration diagram of an embodiment of the present invention, and FIG. 2 is a sectional view of the main part. An untreated oil inlet pipe 20 is provided to the centrifugal separator 10, and an overflow oil recovery pipe 30 and an oil transport pipe 40 to the filter 4 are provided from the centrifuge 10.

前記遠心分離機10には、ケース12内に、モータ等の
回転駆動源11によって回転される遠心分離室13と、
該遠心分離室13と一緒に回転されるポンプ室14が設
けられている。前記遠心分離室13は容器状ケース13
a内に構成されており、該容器状ケース13aの中心軸
が回転軸Xとなっている。そしてこのケース13aの中
心軸でもある回転軸Xに一致する形で、前記ケース12
の天井を貫通して前記未処理油の導入管20が垂下し、
その下端の油放出口20aを分離室13内中央下部に位
置づけている。
The centrifugal separator 10 includes a centrifugal separation chamber 13 within a case 12, which is rotated by a rotational drive source 11 such as a motor;
A pump chamber 14 is provided which rotates together with the centrifugation chamber 13. The centrifugation chamber 13 is a container-like case 13
The central axis of the container-shaped case 13a is the rotation axis X. Then, the case 12
The untreated oil introduction pipe 20 hangs down through the ceiling of the
The oil discharge port 20a at the lower end is located at the lower center of the separation chamber 13.

前記ポンプ室14は前記遠心分離室13の真上に接金さ
れる形で設けられており、遠心分離室13の回転に伴っ
て一緒に回転軸Xを中心に回転するようになされている
。そしてポンプ室14のケース14aの底壁には前記遠
心分離室13内から上昇してくる油を受は入れるための
開口14bが設けられ、またポンプ室14の天井にはオ
ーバーフロー開口14cが設けられている。このオーバ
ーフロー開口14c及び開口14bの中央を通って、前
記導入管20が遠心分離室13内まで垂下している。ま
た前記濾過機4への油輸送管40の基端側吸込口41が
ポンプ室14内に開口されている。吸込口41はポンプ
室14内の側壁近くに側方に向けて開口されている。す
なわちポンプ室14内の圧力の高い位置に開口されてい
る。
The pump chamber 14 is provided directly above the centrifugal separation chamber 13 in a welded manner, and is adapted to rotate around the rotation axis X together with the rotation of the centrifugal separation chamber 13. An opening 14b is provided in the bottom wall of the case 14a of the pump chamber 14 to receive oil rising from the centrifugal separation chamber 13, and an overflow opening 14c is provided in the ceiling of the pump chamber 14. ing. The introduction pipe 20 hangs down into the centrifugation chamber 13 through the center of the overflow opening 14c and the opening 14b. Further, a suction port 41 on the base end side of the oil transport pipe 40 to the filter 4 is opened into the pump chamber 14 . The suction port 41 is opened toward the side near the side wall inside the pump chamber 14 . That is, it is opened at a position within the pump chamber 14 where the pressure is high.

前記遠心分離機lOのケース12内にはオーバーフロー
油の受は溝15が設けられている。ポンプ室14の天井
の開口14cからオーバーフローした油は該受は溝15
で受けられ、さらに回収管30に流れてゆく。
A groove 15 is provided in the case 12 of the centrifugal separator 10 to receive overflow oil. The oil overflowing from the opening 14c in the ceiling of the pump chamber 14 is drained into the groove 15.
The water is received by the pipe 30 and further flows into the collection pipe 30.

今、回転駆動源11が駆動開始され、導入管20を通っ
て未処理の油が導入開始されると、遠心分離室13及び
ポンプ室14が回転し、これにより導入された油が遠心
力を受ける。この遠心力により遠心分離室13内で粗混
入物が油から分離される。そして遠心分離室13には油
が引き続いて導入されるので、その液位が増大し、遠心
分離された油が順次開口14bを通ってポンプ室14内
に入ってゆく。このポンプ室14内に入った油も引き続
き大きな遠心力を受け、外側へ行く程大きな圧力を生じ
る。この高圧力により、ポンプ室14内の油が前記吸込
口41から油輸送管40内に押し出されて、濾過機4ま
で運ばれる。濾過機4に運ばれた油は、そこで遠心分離
されなかった微細混入物が濾過される。これにより油が
清浄化される。
Now, when the rotational drive source 11 is started to drive and untreated oil begins to be introduced through the introduction pipe 20, the centrifugal separation chamber 13 and the pump chamber 14 rotate, and the introduced oil is thereby subjected to centrifugal force. receive. This centrifugal force separates the crude contaminants from the oil in the centrifugal separation chamber 13. As oil is continuously introduced into the centrifugal separation chamber 13, the liquid level increases, and the centrifuged oil sequentially enters the pump chamber 14 through the opening 14b. The oil that has entered the pump chamber 14 continues to be subjected to a large centrifugal force, and the further outward it goes, the greater the pressure is generated. Due to this high pressure, the oil in the pump chamber 14 is pushed out from the suction port 41 into the oil transport pipe 40 and is carried to the filter 4. The oil conveyed to the filter 4 is filtered there from fine contaminants that have not been centrifuged. This cleans the oil.

前記遠心分離機10の回転数が一定であれば、前記ポン
プ室14内における油輸送管吸込口41付近での油圧力
もほぼ一定となり、輸送圧を整えるための特別の圧力調
整弁を必要としない。濾過機4に目詰まりが生じて、濾
過油量が低下してくると、ポンプ室14の液位がまし、
やがてポンプ室14から油がオーバーフローするように
なるが、オーバーフロー流量センサを回収管30に設け
ることにより、濾過機4のメンテナンス時期を容易に知
ることができる。
If the rotation speed of the centrifugal separator 10 is constant, the hydraulic pressure near the oil transport pipe suction port 41 in the pump chamber 14 is also approximately constant, and a special pressure regulating valve is not required to adjust the transport pressure. do not. When the filter 4 becomes clogged and the amount of filtered oil decreases, the liquid level in the pump chamber 14 will increase.
Oil will eventually overflow from the pump chamber 14, but by providing an overflow flow rate sensor in the recovery pipe 30, it is possible to easily know when it is time for maintenance of the filter 4.

なお、遠心分離室13に直接油輸送管40の吸込口41
を設けることも可能である。が、この場合には前記吸込
口41の存在により、油が掻き混ぜられ、遠心分離の効
果が悪くなる。
Note that the suction port 41 of the oil transport pipe 40 is directly connected to the centrifugal separation chamber 13.
It is also possible to provide However, in this case, due to the presence of the suction port 41, the oil is agitated and the effect of centrifugation becomes worse.

〈効果〉 本発明は以上の構成よりなり、請求項1に記載の油清浄
装置によれば、遠心分離機で発生する遠心力をポンプ作
用に兼用して遠心分離後の油を濾過機に送るよう構成し
たので、濾過機への輸送用のポンプや輸送用の油を一旦
貯えるタンク等を別に必要とせず、コストダウン、省エ
ネルギー、省スペースを図ることができる。
<Effects> The present invention has the above configuration, and according to the oil purifying device according to claim 1, the centrifugal force generated in the centrifuge is also used as a pumping action to send the centrifuged oil to the filter. With this configuration, there is no need for a separate pump for transporting oil to the filter, a tank for temporarily storing oil for transport, etc., and it is possible to reduce costs, save energy, and save space.

また請求項2に記載の油清浄装置によれば、請求項1に
記載の構成による効果に加えて、ポンプ室と遠心分離室
とを同一回転軸上に設けているので、遠心力のポンプ作
用への兼用がごく簡単な構成で実現することができる。
Further, according to the oil purifying device according to claim 2, in addition to the effects achieved by the configuration according to claim 1, since the pump chamber and the centrifugal separation chamber are provided on the same rotation axis, the pump action of centrifugal force This can be achieved with a very simple configuration.

しかもポンプ室と遠心分離室とは別室にして設けられて
いるので、ポンプ室でのポンプ動作に必要な部材が遠心
分離室での遠心分離動作ないし作用に悪影響を及ぼすこ
ともない。
Moreover, since the pump chamber and the centrifugal separation chamber are provided as separate rooms, the members necessary for the pump operation in the pump chamber do not adversely affect the centrifugal separation operation or operation in the centrifugal separation chamber.

また請求項3に記載の油清浄装置によれば、ポンプ室上
部が開放されて、オーバーフローできるようになされて
いるので、濾過機の側に目詰まり等が生じることがあっ
ても、それによる影響は前記ポンプ室内の油がオーバー
フローすることによって解消され、回転軸や回転駆動手
段に無理な負荷が加わることがない。また油輸送のため
の圧力調整弁等を必要としない。勿論オーバーフロー油
は回収手段で回収されるので、問題はない。その他、オ
ーバーフロー油の流量を検出することで、濾過機の状態
を知ることができ、メンテナンスを容易に行うことが可
能となる。
Furthermore, according to the oil purifying device according to claim 3, the upper part of the pump chamber is opened to allow overflow, so even if clogging or the like occurs on the side of the filter, there will be no effect from it. This is resolved by overflowing the oil in the pump chamber, and no unreasonable load is applied to the rotating shaft or rotational drive means. Furthermore, there is no need for a pressure regulating valve or the like for transporting oil. Of course, since the overflow oil is recovered by the recovery means, there is no problem. Additionally, by detecting the flow rate of overflow oil, the condition of the filter can be known, making maintenance easier.

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

第1図は本発明実施例の全体構成図、第2図は要部の断
面図、第3図は従来装置の構成図である。 4:濾過機 10:遠心分離機 11:回転駆動源 13:遠心分離室 14:ポンプ室 15:受は溝 20:未処理油の導入管 30ニオ−バーフロー油の回収管 40:油輸送管 41:吸込口 X:回転軸
FIG. 1 is an overall configuration diagram of an embodiment of the present invention, FIG. 2 is a sectional view of the main parts, and FIG. 3 is a configuration diagram of a conventional device. 4: Filter machine 10: Centrifugal separator 11: Rotation drive source 13: Centrifugal separation chamber 14: Pump chamber 15: Receiving groove 20: Untreated oil introduction pipe 30 Ni-bar flow oil recovery pipe 40: Oil transport pipe 41: Suction port X: Rotating shaft

Claims (3)

【特許請求の範囲】[Claims] (1)、油中の粗混入物を遠心分離する遠心分離機と、
輸送されてくる遠心分離後の油から微細混入物を濾過す
る濾過機とを少なくとも有し、前記遠心分離機で発生す
る遠心力をポンプ作用に兼用して遠心分離後の油を前記
濾過機に送るよう構成したことを特徴とする油清浄装置
(1) A centrifugal separator for centrifuging crude contaminants in oil;
and a filter for filtering fine contaminants from the centrifuged oil being transported, and the centrifugal force generated by the centrifugal separator is also used as a pumping action to transfer the centrifuged oil to the filter. An oil purifying device characterized in that it is configured to transmit oil.
(2)、遠心分離後の油を濾過機へ送るためのポンプ室
と遠心分離室とを同一回転軸上に別室にして設けた請求
項1に記載の油清浄装置。
(2) The oil cleaning device according to claim 1, wherein a pump chamber for sending centrifuged oil to a filter and a centrifugal separation chamber are provided as separate chambers on the same rotating shaft.
(3)、ポンプ室上部は開放されており、オーバーフロ
ー油の回収手段が設けられている請求項2に記載の油清
浄装置。
(3) The oil cleaning device according to claim 2, wherein the upper part of the pump chamber is open and a means for collecting overflow oil is provided.
JP1203514A 1989-08-04 1989-08-04 Oil purifier Expired - Lifetime JP2886190B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1203514A JP2886190B2 (en) 1989-08-04 1989-08-04 Oil purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1203514A JP2886190B2 (en) 1989-08-04 1989-08-04 Oil purifier

Publications (2)

Publication Number Publication Date
JPH0368407A true JPH0368407A (en) 1991-03-25
JP2886190B2 JP2886190B2 (en) 1999-04-26

Family

ID=16475414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1203514A Expired - Lifetime JP2886190B2 (en) 1989-08-04 1989-08-04 Oil purifier

Country Status (1)

Country Link
JP (1) JP2886190B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6058899A (en) * 1996-02-20 2000-05-09 Filterwerk Mann & Hummel Gmbh Separator
JP2012081446A (en) * 2010-10-14 2012-04-26 Mitsui O S K Lines Ltd Oil cleaning apparatus and oil cleaning method
CN103801148A (en) * 2013-11-01 2014-05-21 昆山威胜达环保设备有限公司 Novel vacuum centrifugal-separation oil purifier
JP2015006666A (en) * 2013-06-24 2015-01-15 エスケイエフ ルーブリケイション システムズ ジャーマニー アクチエンゲゼルシャフトSKF Lubrication Systems Germany AG Lubricant filter unit and lubrication system including the same
US10384215B2 (en) 2013-12-02 2019-08-20 Gm Innovations Limited Centrifugal separator for removing impurities from a fluid stream
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JP2012081446A (en) * 2010-10-14 2012-04-26 Mitsui O S K Lines Ltd Oil cleaning apparatus and oil cleaning method
JP2015006666A (en) * 2013-06-24 2015-01-15 エスケイエフ ルーブリケイション システムズ ジャーマニー アクチエンゲゼルシャフトSKF Lubrication Systems Germany AG Lubricant filter unit and lubrication system including the same
CN103801148A (en) * 2013-11-01 2014-05-21 昆山威胜达环保设备有限公司 Novel vacuum centrifugal-separation oil purifier
US10384215B2 (en) 2013-12-02 2019-08-20 Gm Innovations Limited Centrifugal separator for removing impurities from a fluid stream
US11857982B2 (en) 2017-02-27 2024-01-02 Gm Innovations Limited Apparatus with axially movable wall member for separating components of a fluid stream
US11975341B2 (en) 2018-03-26 2024-05-07 Gm Innovations Limited Apparatus for separating components of a fluid stream
US11840469B2 (en) 2018-04-24 2023-12-12 Gm Innovations Limited Apparatus for producing potable water

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