JP2886190B2 - Oil purifier - Google Patents

Oil purifier

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Publication number
JP2886190B2
JP2886190B2 JP1203514A JP20351489A JP2886190B2 JP 2886190 B2 JP2886190 B2 JP 2886190B2 JP 1203514 A JP1203514 A JP 1203514A JP 20351489 A JP20351489 A JP 20351489A JP 2886190 B2 JP2886190 B2 JP 2886190B2
Authority
JP
Japan
Prior art keywords
oil
chamber
pump chamber
centrifugal separation
separation 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.)
Expired - Lifetime
Application number
JP1203514A
Other languages
Japanese (ja)
Other versions
JPH0368407A (en
Inventor
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)

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 purifying apparatus that can be used for purifying lubricating oil for a diesel engine, for example.

<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 cleaning apparatus. 1 is a centrifugal separator, 2 is an oil tank, 3 is a transport pump, and 4 is a filter. The used oil is introduced into the centrifuge 1 from 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 and further pumped up by a transport pump 3 and sent to a filter 4, where residual fine contaminants are filtered.

<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、さらに別に設けられた輸送
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 above-described conventional apparatus, the oil that has passed through the centrifugal separator is temporarily stored in the oil tank 2 and is sent to the filter 4 by the transport pump 3 provided separately. Because
The transport pump 3 and a motor for driving the transport pump 3 are required, and there is a disadvantage that running costs and the like are increased. There is also a drawback that the oil tank 2 must 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。
Accordingly, an object of the present invention is to provide an oil purifying apparatus which can solve the above-mentioned drawbacks of the conventional apparatus, can save energy and space, and can have a simple configuration by using fewer members.

<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、導
入管20を通って遠心分離室13内に供給された未処理油か
ら油中の粗混入物を遠心分離するための遠心分離機10
と、該遠心分離機10から油輸送管40を通って運ばれてく
る粗混入物除去後の油から微細混入物を濾過するための
濾過機4とを少なくとも有する油清浄装置であって、前
記遠心分離機10には、回転軸Xを中心として水平回転さ
れる容器状の遠心分離室13を構成すると共に、該遠心分
離室13の直上に、該遠心分離室13とは仕切り壁14dで室
を仕切られたポンプ室14を構成し、該ポンプ室14には、
前記仕切り壁14dの中央部に開口14bを設けて前記遠心分
離室13の中心軸X付近にある油のみがポンプ室14へ流入
されるように構成すると共に、ポンプ室14内空間の側壁
近くに前記油輸送管40の吸込口41を開口させることで、
前記粗混入物除去後の油がポンプ室14内から前記濾過機
4に運ばれるように構成したことを特徴としている。
<Means for Solving the Problems> In order to achieve the above object, the oil cleaning device of the present invention removes crude contaminants in oil from untreated oil supplied into the centrifugal separation chamber 13 through the introduction pipe 20. Centrifuges 10 for centrifugation
An oil purifier having at least a filter 4 for filtering fine contaminants from the oil from which coarse contaminants have been removed, which are conveyed from the centrifuge 10 through the oil transport pipe 40, The centrifugal separator 10 includes a container-like centrifugal separation chamber 13 that is horizontally rotated around the rotation axis X, and has a partition wall 14d just above the centrifugal separation chamber 13 and the centrifugal separation chamber 13. The pump chamber 14 is partitioned, and the pump chamber 14 includes:
An opening 14b is provided at the center of the partition wall 14d so that only oil near the center axis X of the centrifugal separation chamber 13 flows into the pump chamber 14, and near the side wall of the space inside the pump chamber 14. By opening the suction port 41 of the oil transport pipe 40,
It is characterized in that the oil after the removal of the coarse contaminants is carried from the inside of the pump chamber 14 to the filter 4.

<作用> 上記本発明の第1の特徴によれば、導入管20を通って
遠心分離機10の容器状の遠心分離室13に供給された未処
理油は、遠心分離室13の回転により、その粗混入物が遠
心分離室13内の周縁方向に遠心分離される。そして該粗
混入物が除去された遠心分離室13の中央付近の油は仕切
り壁14d中央部の開口14bからポンプ室14に流入する。遠
心分離室13の中央付近以外の場所にある油(粗混入物が
混じっている油)は仕切り壁14dによって部屋を仕切ら
れたポンプ室14内には入って行くことができない。
<Operation> According to the first feature of the present invention, the untreated oil supplied to the container-like centrifugal separation chamber 13 of the centrifuge 10 through the introduction pipe 20 is rotated by the rotation of the centrifuge chamber 13. The coarse contaminants are centrifuged in the peripheral direction in the centrifuge chamber 13. The oil near the center of the centrifugal separation chamber 13 from which the coarse contaminants have been removed flows into the pump chamber 14 through the opening 14b at the center of the partition wall 14d. Oil (oil mixed with coarse contaminants) other than near the center of the centrifugal separation chamber 13 cannot enter the pump chamber 14 partitioned by the partition wall 14d.

前記ポンプ室14内に流入した油(粗混入物が除去され
た油)はポンプ室14内空間の側壁近くに配置された吸込
口41から油輸送管40を通って濾過機4に運ばれ、更に微
細混入物が除去される。
The oil flowing into the pump chamber 14 (oil from which coarse contaminants have been removed) is conveyed to the filter 4 through an oil transport pipe 40 from a suction port 41 arranged near a side wall of the space inside the pump chamber 14, Further, fine contaminants are removed.

以上の作用により、遠心分離後の油を一旦溜めるため
のタンクが不要となる。
By the above operation, a tank for temporarily storing oil after centrifugation is not required.

また、遠心分離機10の回転駆動を利用してポンプ室14
のポンプ動作を行わせることができるので、ポンプを必
要とせず、装置の構成が簡単となる。
Further, the pump chamber 14 is rotated by using the rotational drive of the centrifuge 10.
Can be performed, so that no pump is required and the configuration of the apparatus is simplified.

特に、遠心分離室13とその上にあるポンプ室14とを仕
切り壁14dで仕切ることで、遠心分離室13内の粗混入物
が含まれた油がポンプ室14に入ってこないようにすると
共に中央部の開口14bからのみ粗混入物が除かれた油を
ポンプ室14内に導入し、そこから改めて粗混入物が除か
れた油を濾過機4に送るようにしているので、濾過機4
には粗混入物が十分に除かれた油のみを確実に送って、
微細混入物の濾過に供することができる。
In particular, by separating the centrifugal separation chamber 13 and the pump chamber 14 above it with the partition wall 14d, oil containing coarse contaminants in the centrifuge separation chamber 13 is prevented from entering the pump chamber 14. The oil from which the coarse contaminants have been removed is introduced into the pump chamber 14 only through the opening 14b at the center, and the oil from which the coarse contaminants have been removed is sent to the filter 4 again.
Surely send only oil from which crude contaminants have been sufficiently removed,
It can be used for filtration of fine contaminants.

<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への油油送管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 a main part. Untreated oil inlet tube for centrifuge 10
A centrifuge 10 is provided with a recovery pipe 30 for overflow oil and an oil feed pipe 40 to the filter 4.

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13a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 is provided in a case 12 with a centrifugal separation chamber 13 rotated by a rotary drive source 11 such as a motor, and a pump chamber 14 rotated together with the centrifugal separation chamber 13. The centrifugal separation chamber 13 is formed in a container-like case 13a, and the central axis of the container-like case 13a is the rotation axis X. And the rotation axis X which is also the center of this case 13a
The untreated oil introduction pipe 20 hangs down through the ceiling of the case 12 in such a manner that the oil discharge port 20a at the lower end thereof is positioned at the lower center in the separation chamber 13.

前記ポンプ室14は前記遠心分離室13の真上に接合され
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の底壁を前記遠心分離室13
との仕切り壁14dとして、ポンプ室14を遠心分離室13か
ら仕切るようにすると共に、前記回転軸Xが通る仕切り
壁14dの中央部に開口14bを設けて、前記遠心分離室13内
から上昇してくる油を受け入れるようにしている。この
開口14bからは前記遠心分離室13内の中央付近にあって
粗混入物が遠心除去された油のみがポンプ室14に流入さ
れ、粗混入物の含まれた油は仕切り壁14dに阻まれて、
ポンプ室14には入ることができない。
The pump chamber 14 is provided directly above the centrifugal separation chamber 13 so as to rotate together with the rotation axis X as the centrifuge chamber 13 rotates. Then, the bottom wall of the case 14a of the pump chamber 14 is
As the partition wall 14d, the pump chamber 14 is partitioned from the centrifugal separation chamber 13, and an opening 14b is provided at the center of the partition wall 14d through which the rotation axis X passes. We accept incoming oil. From this opening 14b, only the oil near the center of the centrifugal separation chamber 13 from which the coarse contaminants have been centrifugally removed flows into the pump chamber 14, and the oil containing the coarse contaminants is blocked by the partition wall 14d. hand,
The pump room 14 cannot enter.

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1
4b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。
An overflow opening 14c is provided in the ceiling of the pump room 14. This overflow opening 14c and opening 1
Through the center of 4b, the introduction tube 20 hangs down into the centrifugation chamber 13. Further, a suction port 41 on the base end side of the oil transport pipe 40 to the filter 4 is opened in the pump chamber 14. Suction port 41
Is opened to the side near the side wall in the pump chamber 14. That is, the pump chamber 14 is opened at a high pressure position.

前記遠心分離機10のケース12内にはオーバーフロー油
の受け溝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け溝15で受けら
れ、さらに回収管30に流れてゆく。
A receiving groove 15 for overflow oil is provided in the case 12 of the centrifuge 10. Opening of ceiling of pump room 14
The oil overflowing from 14c is received in the receiving groove 15, and further flows into the recovery 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
油が順次中央の開口14bを通ってポンプ室14内に入って
ゆく。粗混入物を含む油は遠心分離室13内の周縁付近に
あって、仕切り壁14dに阻まれ、ポンプ室14には入って
行くことができない。
Now, when the rotation drive source 11 is started to drive and the untreated oil is introduced through the introduction pipe 20, the centrifugal separation chamber 13 and the pump chamber 14 rotate, whereby the introduced oil reduces the centrifugal force. receive. This centrifugal force separates the crude contaminants from the oil in the centrifugation chamber 13. Then, the oil is continuously introduced into the centrifugal separation chamber 13, so that the liquid level increases, and the centrifugally separated oil sequentially enters the pump chamber 14 through the central opening 14b. The oil containing the coarse contaminants is located near the periphery in the centrifugal separation chamber 13 and is blocked by the partition wall 14d and cannot enter the pump chamber 14.

前記ポンプ室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内にあって粗混入物が除かれた油
は、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。
The oil that has entered the pump chamber 14 is also continuously subjected to a large centrifugal force, and generates a large pressure outward. Due to the high pressure, the oil in the pump chamber 14 from which the coarse contaminants have been removed is pushed out from the suction port 41 into the oil transport pipe 40 and carried to the filter 4. The oil conveyed to the filter 4 is filtered for fine contaminants that have not been centrifuged there. 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収口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の液位が増し、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 oil pressure near the oil transport pipe absorption port 41 in the pump chamber 14 becomes almost constant, and a special pressure regulating valve for adjusting the transport pressure is required. do not do. When the amount of filtered oil decreases due to clogging of the filter 4, the liquid level in the pump chamber 14 increases, and oil eventually overflows from the pump chamber 14.
By providing the overflow flow sensor in the recovery pipe 30, the maintenance time of the filter 4 can be easily known.

<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10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4に送ること
ができるので、濾過機4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。
<Effect> According to the oil purifier of the first aspect of the present invention, the centrifugal force generated by the centrifugal separator 10 is also used as a pump action to filter the oil after centrifugal separation. Therefore, it is not necessary to separately provide a pump for transportation to the filter 4 or a tank for temporarily storing oil for transportation, and cost reduction, energy saving, and space saving can be achieved.

またポンプ室14を遠心分離室13の直上に構成している
ので、遠心力のポンプ作用への兼用をごく簡単な構成で
実現することができる。
In addition, since the pump chamber 14 is configured immediately above the centrifugal separation chamber 13, it is possible to realize the dual use of the centrifugal force for the pump action with a very simple configuration.

特に、ポンプ室14と遠心分離室13とは仕切り壁14dに
よって別室にし、粗混入物を含んだ油がポンプ室14に入
ってくるのを阻止すると共に、仕切り壁14dの中央に設
けた開口14bからのみ遠心分離室13内の油がポンプ14内
に入るようにしているので、遠心分離室13内の中央付近
の粗混入物が十分に除去された油だけをポンプ室14に導
き入れ、濾過機4に向けて供給することができる。
In particular, the pump chamber 14 and the centrifugal separation chamber 13 are separated from each other by a partition wall 14d to prevent oil containing coarse contaminants from entering the pump chamber 14, and an opening 14b provided in the center of the partition wall 14d. Only the oil in the centrifugal separation chamber 13 is allowed to enter the pump 14, so only the oil from the center of the centrifuge separation chamber 13 where the coarse contaminants have been sufficiently removed is introduced into the pump chamber 14 and filtered. Machine 4 can be supplied.

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

第1図は本発明の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 14b:開口 14d:仕切り壁 15:受け溝 20:未処理油の導入管 30:オーバーフロー油の回収管 40:油輸送管 41:吸込口 X:回転軸
1 is an overall configuration diagram of an embodiment of the present invention, FIG. 2 is a cross-sectional view of a main part, and FIG. 3 is a configuration diagram of a conventional device. 4: Filtration machine 10: Centrifuge 11: Rotary drive source 13: Centrifugal separation chamber 14: Pump chamber 14b: Opening 14d: Partition wall 15: Receiving groove 20: Untreated oil introduction pipe 30: Overflow oil recovery pipe 40 : Oil transport pipe 41: Suction port X: Rotating axis

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】導入管20を通って遠心分離室13内に供給さ
れた未処理油から油中の粗混入物を遠心分離するための
遠心分離機10と、該遠心分離機10から油輸送管40を通っ
て運ばれてくる粗混入物除去後の油から微細混入物を濾
過するための濾過機4とを少なくとも有する油清浄装置
であって、前記遠心分離機10には、回転軸Xを中心とし
て水平回転される容器状の遠心分離室13を構成すると共
に、該遠心分離室13の直上に、該遠心分離室13とは仕切
り壁14dで室を仕切られたポンプ室14を構成し、該ポン
プ室14には、前記仕切り壁14dの中央部に開口14bを設け
て前記遠心分離室13の中心軸X付近にある油のみがポン
プ室14へ流入されるように構成すると共に、ポンプ室14
内空間の側壁近くに前記油輸送管40の吸込口41を開口さ
せることで、前記粗混入物除去後の油がポンプ室14内か
ら前記濾過機4に運ばれるように構成したことを特徴と
する油清浄装置。
1. A centrifuge 10 for centrifuging crude contaminants in oil from an untreated oil supplied into a centrifugation chamber 13 through an introduction pipe 20, and oil transport from the centrifuge 10. An oil purifier having at least a filter 4 for filtering fine contaminants from the oil after coarse contaminants removed through the pipe 40, wherein the centrifugal separator 10 has a rotating shaft X Constitute a container-shaped centrifugal separation chamber 13 that is horizontally rotated around the center, and a pump chamber 14 separated from the centrifugal separation chamber 13 by a partition wall 14d immediately above the centrifugal separation chamber 13. The pump chamber 14 is provided with an opening 14b at the center of the partition wall 14d so that only oil near the center axis X of the centrifugal separation chamber 13 flows into the pump chamber 14. Room 14
The suction port 41 of the oil transport pipe 40 is opened near the side wall of the inner space, so that the oil after the removal of the coarse contaminants is carried from the pump chamber 14 to the filter 4. Oil purifying equipment.
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 JPH0368407A (en) 1991-03-25
JP2886190B2 true 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

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