JPH0278454A - Centrifugal electrostatic oil cleaner - Google Patents

Centrifugal electrostatic oil cleaner

Info

Publication number
JPH0278454A
JPH0278454A JP63231316A JP23131688A JPH0278454A JP H0278454 A JPH0278454 A JP H0278454A JP 63231316 A JP63231316 A JP 63231316A JP 23131688 A JP23131688 A JP 23131688A JP H0278454 A JPH0278454 A JP H0278454A
Authority
JP
Japan
Prior art keywords
oil
electrode plate
oil tank
lowermost
drain system
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
Application number
JP63231316A
Other languages
Japanese (ja)
Inventor
Sakae Sanada
真田 栄
Kenichi Fukada
健一 深田
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.)
Mitsubishi Agricultural Machinery Co Ltd
Original Assignee
Mitsubishi Agricultural Machinery Co Ltd
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 Mitsubishi Agricultural Machinery Co Ltd filed Critical Mitsubishi Agricultural Machinery Co Ltd
Priority to JP63231316A priority Critical patent/JPH0278454A/en
Publication of JPH0278454A publication Critical patent/JPH0278454A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/04Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B5/00Other centrifuges
    • B04B5/10Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges

Landscapes

  • Electrostatic Separation (AREA)
  • Centrifugal Separators (AREA)

Abstract

PURPOSE:To allow easy sinking of inclusions down to a drain system and to improve cleaning efficiency by surely guiding the oil which is to be cleaned and is ejected from an ejection port to the upper part of the drain system in the bottom of an oil tank by bevel electrode plate near the lowermost stage which is not provided with holes. CONSTITUTION:Oil feed and drain systems 21, 33 which run the oil to be cleaned upward from the ejection port 27 near the bottom of the rotary oil tank 5 are constituted of a shaft 19 which is provided in the rotary oil tank 5, the plural bevel electrode plates 23 which are laminated and installed at prescribed intervals to the shaft 19 and are bored with the holes 23a, the electrode 31 which is provided on the inner wall surface of the rotary oil tank 5 and is different in pole from the plates 23, and the ejection port 27 which is provided on the lower side of the conical electrode plate 25 of the lowermost stage and ejects the oil to be cleaned. The drain system 35 which stagnate and discharge the inclusions is provided to the lower side of the oil feed and discharge systems 21, 33. The plate 25 near the lowermost stage is not provided with holes. As a result, the inclusions are easily sunk down into the drain system and the higher cleaning efficiency than heretofore is obtd.

Description

【発明の詳細な説明】 〈産業上の利用分野)・ この発明は遠心静電浄油機にかかり、詳しくは浄化効率
を上げるための該浄油機の内部構造に関するものである
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a centrifugal electrostatic oil purifier, and specifically relates to the internal structure of the oil purifier for increasing purification efficiency.

く従来の技術〉 従来、遠心静電浄油機においては、特公昭57−614
60号公報に記載されているように、油槽の回転によっ
て水分及び質量の大きい粒子を遠心沈降させるとともに
、質量の小さい粒子は静電分離して、汚染油中の汚染粒
子等を分離できるように構成されており、一般に回転す
る浄化油槽内で分離された汚染粒子等は、比重の差によ
って下方に沈下し、浄(ヒ油槽の下側に配置されている
ドレン系内に回収されるものである。
Conventional technology> Conventionally, in centrifugal electrostatic oil purifiers,
As described in Publication No. 60, water and particles with large mass are centrifugally sedimented by rotation of the oil tank, and particles with small mass are electrostatically separated, so that contaminant particles in contaminated oil can be separated. Contaminant particles, etc. separated in the rotating purifying oil tank generally sink downward due to the difference in specific gravity and are collected in the drain system located below the purifying oil tank. be.

〈発明が解決しようとする課題〉 しかし、上記従来の遠心静電浄油機においては、回転す
る浄油機の回転中心に積層設置された全電極板の形状は
全部が略等しく構成されている。
<Problems to be Solved by the Invention> However, in the conventional centrifugal electrostatic oil purifier described above, the shapes of all the electrode plates stacked and installed at the rotation center of the rotating oil purifier are all approximately the same. .

このため、最下段の全電極板の下側に設けられている噴
出口から浄油すべき油を噴出すると、油内の汚染粒子の
中には遠心力が大きくなる回転油槽の周壁付近l\達す
ることなく、油の上昇流とともに全電極板に設けられた
孔を通って上昇してしまうものがあり、これらの汚染粒
子は遠心分離されてドレン系へ沈下する前に浄油機から
排出されてしまうといった課題があった。
For this reason, when the oil to be purified is ejected from the spout ports provided below all the electrode plates at the lowest stage, some of the contaminant particles in the oil are near the peripheral wall of the rotary oil tank where centrifugal force increases. Some contaminant particles may not reach the oil flow and rise through the holes provided in all electrode plates with the upward flow of oil, and these contaminant particles are discharged from the oil purifier before being centrifuged and settling in the drain system. There were some issues, such as:

く課題を解決するための手段〉 上記のような課題を解決するための本発明は、回転油槽
5内に設けられた軸19と、該軸19に所定間隔で積層
設置され孔23aが穿設された複数の全電極板23と、
前記回転油槽5内側壁面に設けられた前記全電極板23
と異様となる電極31と、最下段の全電極板25下側に
設けられた浄化すべき油を噴出する噴出口27とによっ
て、回転油槽5の底部近傍噴出口27から浄化すべき油
を上方I\流動させる給排油系21.33を構成し、前
記給排油系21.33の下側には混入物を滞留排出する
ドレン系35を設けた構造において、最下段近傍の全電
極板25を無孔としたことを特徴とし、また第2の手段
としては上記手段において該最下段傘電極板37と噴出
口27との間には噴出した浄化すべき油の上方流動を規
制するガイド部材39を設け、該ガイド部材39の周縁
が対向する部位より下方の上記最下段傘電極板37を無
孔とし、前記ガイド部材39の周縁が対向する部位より
上方の上記最下段傘電極板37に孔37aを穿設したこ
とを特徴としている。
Means for Solving the Problems> The present invention for solving the above problems consists of a shaft 19 provided in the rotary oil tank 5, a shaft 19 stacked at predetermined intervals, and holes 23a drilled therein. a plurality of all electrode plates 23,
The full electrode plate 23 provided on the inner wall surface of the rotary oil tank 5
The oil to be purified is discharged upward from the spout 27 near the bottom of the rotary oil tank 5 by the electrode 31 that has a strange shape and the spout 27 that spouts out the oil to be purified, which is provided below the lowermost electrode plate 25. I\In a structure in which an oil supply and drainage system 21.33 for fluidization is configured, and a drain system 35 for retaining and discharging contaminants is provided below the oil supply and drainage system 21.33, all electrode plates near the lowest stage 25 is non-porous, and as a second means, a guide is provided between the lowermost umbrella electrode plate 37 and the spout 27 to regulate the upward flow of the oil to be purified that has spouted out. A member 39 is provided, the lowermost umbrella electrode plate 37 below the area where the periphery of the guide member 39 faces is made non-porous, and the lowermost umbrella electrode plate 37 above the area where the periphery of the guide member 39 faces. It is characterized in that a hole 37a is bored in the hole 37a.

く作用〉 給油系21から送られる浄化すべき油は噴出口27から
油槽5内に送られる。油槽5内の油は油槽5の回転によ
って遠心方向l\移動するとともに、最下段の全電極板
25によって下方へ案内される。
Effect> Oil to be purified sent from the oil supply system 21 is sent into the oil tank 5 from the spout 27. The oil in the oil tank 5 is moved in the centrifugal direction l\ by the rotation of the oil tank 5, and is guided downward by all the electrode plates 25 at the lowest stage.

ここで最下段傘電極板25は無孔であるため、油は遠心
力が最も大となる全電極板25の周縁部分まで確実に移
動し質量の大きい混入物は遠心分離される。
Here, since the lowermost umbrella electrode plate 25 is non-porous, the oil reliably moves to the peripheral portion of all the electrode plates 25 where the centrifugal force is greatest, and contaminants with large mass are centrifugally separated.

上方へ流動する油は全電極板23の孔23aを通って更
に上方の排油系33から排出される。油中の微少粒子は
全電極板23.25によって帯電され、油槽5の内壁に
もうけられた電極31に吸着分離される。
The oil flowing upward passes through the holes 23a of all the electrode plates 23 and is further discharged from the oil drainage system 33 located above. The microparticles in the oil are charged by all the electrode plates 23 and 25, and are adsorbed and separated by the electrodes 31 provided on the inner wall of the oil tank 5.

また特許請求の範囲第2項記載の発明においては、噴出
口27から流れ込んだ浄化すべき油はガイド部材39に
よって遠心方向に移動し、最下段傘電極板37に当たっ
たところで遠心分離される。そして分離された混入物は
最下段傘電極板37に沿って下方へ移動し、分離によっ
て浄化された油は上方に移動して孔37aから上方l\
流動する。
Further, in the invention as set forth in claim 2, the oil to be purified that has flowed in from the spout 27 is moved in the centrifugal direction by the guide member 39, and is centrifugally separated when it hits the lowermost umbrella electrode plate 37. Then, the separated contaminants move downward along the lowermost umbrella electrode plate 37, and the oil purified by separation moves upward and flows upward from the hole 37a.
Flow.

いずれの場合にも最下段の全電極板35.37で遠心分
離しきれなかった混入物は、油槽5内を上昇流動する際
に遠心分離され、ドレン系35内へ沈降する。
In either case, the contaminants that could not be centrifuged by all the electrode plates 35 and 37 at the lowest stage are centrifuged as they flow upward in the oil tank 5 and settle into the drain system 35.

〈実施例〉 以下図面に基づいて本発明の一実施例の装置について詳
説する。第2図は汚染油を浄化する浄化回路系を示す全
体図である。遠心静電浄油機1は主として移動可能なケ
ース3内に回転自在に支持された油槽5とモータ9とか
らなる。油槽5の下側にはプーリ7が形成され、ベルト
8によってモータ9の駆動力が油槽5に伝わり回転する
<Embodiment> An apparatus according to an embodiment of the present invention will be described in detail below based on the drawings. FIG. 2 is an overall diagram showing a purification circuit system for purifying contaminated oil. The centrifugal electrostatic oil purifier 1 mainly consists of an oil tank 5 rotatably supported within a movable case 3 and a motor 9. A pulley 7 is formed below the oil tank 5, and the drive force of a motor 9 is transmitted to the oil tank 5 by a belt 8, causing it to rotate.

該油槽5の下側にはドレン槽11が設けられ、回転する
油槽5において分離された混入物を回収し、ドレンコッ
ク13より排出される。15.17は異極の電極で、後
述する全電極板23と集塵電極板31とに接続されてい
る。
A drain tank 11 is provided below the oil tank 5, and the contaminants separated in the rotating oil tank 5 are collected and discharged from a drain cock 13. Reference numerals 15 and 17 denote electrodes of different polarities, which are connected to a total electrode plate 23 and a dust collecting electrode plate 31, which will be described later.

第1図は油槽5の断面図である。油槽5の回転中心には
軸19が立設されている。管状の軸19の内側には給油
系21が形成され、軸19の下端には浄化すべき油を噴
出する噴出口27が穿設されている。
FIG. 1 is a sectional view of the oil tank 5. A shaft 19 is erected at the center of rotation of the oil tank 5. An oil supply system 21 is formed inside the tubular shaft 19, and a spout 27 is provided at the lower end of the shaft 19 to spout oil to be purified.

また軸19には複数の全電極板23が所定間隔で積層設
置され、第4図に示すように各全電極板23には複数の
孔23aが穿設され、噴出口27から噴出した油は鎖孔
23aを通過して上方へ流れる。上方に流れた油は、油
槽5内で浄化されて油槽上部の排油系33より排出され
る。
Further, a plurality of all electrode plates 23 are stacked on the shaft 19 at predetermined intervals, and as shown in FIG. It passes through the chain hole 23a and flows upward. The oil flowing upward is purified within the oil tank 5 and discharged from an oil drainage system 33 at the top of the oil tank.

本実施例の装置においては、上記した複数の傘電極板2
3の最下段水電極板25が、第1図及び第5図に示すよ
うに、他の傘電極板23よりも大径となっており、油が
流通する孔も穿設されていない。
In the device of this embodiment, the plurality of umbrella electrode plates 2 described above are used.
As shown in FIGS. 1 and 5, the lowermost water electrode plate 25 of No. 3 has a larger diameter than the other umbrella electrode plates 23, and has no hole through which oil flows.

円筒状の油槽5の内壁29には、所定間隔で集塵電極板
31が軸線方向に取付られている。また油槽5の下方に
は分離された混入物が沈下して回収されるドレン槽11
からなるドレン系35が設けられている。
Dust collecting electrode plates 31 are attached to the inner wall 29 of the cylindrical oil tank 5 at predetermined intervals in the axial direction. Further, below the oil tank 5 is a drain tank 11 in which separated contaminants sink and are collected.
A drain system 35 is provided.

以下第3図に基づいて本実施例特有の構造に基づく1ヤ
用について説明する。給油系21から噴出口27を介し
て噴出した浄化すべき油は、油槽5の回転によって回転
しながら最下段水電極板25に案内されて油槽5の最下
方まで達し、ドレン系35の直上まで移動する。最下段
水電極板25が無孔でかつ大径であるため、第3図矢印
で示すように、油中に含まれている汚染粒子はドレン系
35に近接した真上まで確実に案内される。
Hereinafter, the one-layer use based on the structure unique to this embodiment will be explained based on FIG. The oil to be purified spouted from the oil supply system 21 through the spout 27 is guided by the lowermost water electrode plate 25 while being rotated by the rotation of the oil tank 5, reaches the lowest part of the oil tank 5, and reaches just above the drain system 35. Moving. Since the lowermost water electrode plate 25 is non-porous and has a large diameter, contaminant particles contained in the oil are reliably guided directly above the drain system 35, as shown by the arrow in FIG. .

最下段傘電極板25周端から離れた油は上方へ流れるが
、汚染粒子は遠心力と流線力との合力方向に飛び出し、
ドレン系35の壁面に沿って流れ落ちる。ここで該汚染
粒子は最下段水電極板25によって最下方まで案内され
ているので、油とともに上方へ流れて排油系33から排
出される割合がすくなくなる。また最下段水電極板25
は他の傘電極板23に比べて径が大きいため、遠心力が
最大となる油槽5の周端付近まで総ての浄化すべき油を
確実に送ることができ、より大きな遠心力によって浄化
効率を増すことができる。
The oil that has left the peripheral edge of the lowermost umbrella electrode plate 25 flows upward, but the contaminant particles fly out in the direction of the resultant force of centrifugal force and streamline force.
It flows down along the wall of the drain system 35. Here, since the contaminant particles are guided to the lowest part by the lowermost water electrode plate 25, the proportion of them flowing upward together with the oil and being discharged from the oil drainage system 33 is reduced. In addition, the lowest water electrode plate 25
has a larger diameter than the other umbrella electrode plates 23, so all the oil to be purified can be reliably sent to the vicinity of the peripheral edge of the oil tank 5 where the centrifugal force is maximum, and the greater centrifugal force increases the purification efficiency. can be increased.

また油とともに上方へ押し流された汚染粒子も遠心力に
よって分離され、同じく遠心力によって分離された水分
とともにドレン系35へ沈降する。
Contaminant particles that have been swept upward together with the oil are also separated by the centrifugal force and settle into the drain system 35 together with the water separated by the centrifugal force.

さらに遠心力の比較的小さい回転中心付近の汚染粒子も
傘電極板23によって帯電して、遠心力の大きな油槽5
内周壁にある集塵電極板31まで引き付けられるため、
遠心分離が可能となる。このように油から分離されて沈
降した汚染粒子はドレン系35のドレン槽11へ収容さ
れる。
Furthermore, contaminant particles near the rotation center where the centrifugal force is relatively small are also charged by the umbrella electrode plate 23, and the oil tank 5 where the centrifugal force is large is charged.
Because it is attracted to the dust collecting electrode plate 31 on the inner peripheral wall,
Centrifugation becomes possible. The contaminant particles thus separated from the oil and settled are stored in the drain tank 11 of the drain system 35.

遠心力では分離できない微粒子は従来と同様に傘電極板
25.23によって帯電され、集塵電極板31に引き寄
せられて分離される。
Fine particles that cannot be separated by centrifugal force are charged by the umbrella electrode plates 25 and 23, as in the conventional case, and are attracted to the dust collection electrode plate 31 and separated.

第6図は他の実施例を示す遠心静電浄油機の部分拡大断
面図である。本実施例の構造においては、噴出口27と
最下段水電極板37の間には、第8図のような円盤状の
ガイド部材39が取り付けられている。該ガイド部材3
9によって、噴出口27から噴出した浄化すべき油はガ
イド部材39によって上方への流れが規制され、−旦水
平方向I\流れることとなる。第6図及び第7図に示す
ように、最下段水電極板37には前記ガイド部材39の
周縁に対向する部位より上部に、孔37aが穿設されて
いる。このように構成することによって、ガイド部材3
9によって水平方向へ案内された浄化すべき油は、孔3
7aが穿設されていない最下段水電極板37の下部に当
たる。ここで質量の重い汚染粒子や水は遠心力によって
、最下段水電極板37の下側面に沿って外側に案内され
、分離された油は最下段水電極板37の下面に沿って上
昇し孔37aから上方へ流れ出る。また外側に案内され
た汚染粒子等は上記第1実施例と同様にドレン系35の
真上まで移動して遠心力によって更に分離される。
FIG. 6 is a partially enlarged sectional view of a centrifugal electrostatic oil purifier showing another embodiment. In the structure of this embodiment, a disc-shaped guide member 39 as shown in FIG. 8 is attached between the jet port 27 and the lowermost water electrode plate 37. The guide member 3
9, the oil to be purified spouted from the spout 27 is restricted from flowing upward by the guide member 39, and then flows in the horizontal direction I\. As shown in FIGS. 6 and 7, a hole 37a is formed in the lowermost water electrode plate 37 above a portion facing the periphery of the guide member 39. As shown in FIGS. With this configuration, the guide member 3
The oil to be purified horizontally guided by hole 3
7a corresponds to the lower part of the lowermost water electrode plate 37 where no holes are formed. Here, heavy contaminant particles and water are guided outward along the lower surface of the lowermost water electrode plate 37 by centrifugal force, and the separated oil rises along the lower surface of the lowermost water electrode plate 37 and pores. It flows upward from 37a. In addition, contaminant particles and the like guided to the outside move to just above the drain system 35 and are further separated by centrifugal force, as in the first embodiment.

以上のように構成された遠心静電浄油機1は第2図に示
すように、給油系21と排油系33を汚染油槽41に接
続し、給油系21にはポンプ43を設け、該ポンプ43
によって上記遠心静電浄油機1へ浄化すべき油を送る 排油系33には検査装置47が並列に接続されており、
コック45を開閉することによって検査装置47内に浄
化された油がながれ、該検査装置47によって浄化の程
度が把握される。
As shown in FIG. 2, the centrifugal electrostatic oil purifier 1 configured as described above has an oil supply system 21 and an oil drainage system 33 connected to a contaminated oil tank 41, a pump 43 provided in the oil supply system 21, pump 43
An inspection device 47 is connected in parallel to the oil drain system 33 that sends oil to be purified to the centrifugal electrostatic oil purifier 1.
By opening and closing the cock 45, purified oil flows into the inspection device 47, and the degree of purification is ascertained by the inspection device 47.

第9図(A)(B)及び第10図(A)(B)は検査装
置47の内部構造を示すものである。検査装置47内に
は送油管49が設けられ、該送油管49には検査部51
が取り付けられている。検査部51には投光性を有する
材質からなる透明板57が組み付けられ、光が透過可能
に構成されている。検査部51をはさんで一方には光源
53を取り付け、他方には光センサ−55が配置されて
いる。該光センサ−55は検査部51を通過した光源5
3からの光度を測定することによって油の汚れを測定検
査する。
9(A)(B) and FIG. 10(A)(B) show the internal structure of the inspection device 47. FIG. An oil pipe 49 is provided in the inspection device 47, and an inspection section 51 is installed in the oil pipe 49.
is installed. A transparent plate 57 made of a light-emitting material is attached to the inspection section 51, and is configured to allow light to pass therethrough. A light source 53 is attached to one side of the inspection section 51, and an optical sensor 55 is arranged on the other side. The optical sensor 55 detects the light source 5 that has passed through the inspection section 51.
The oil contamination is measured and tested by measuring the light intensity from 3.

検査部51は第9図(A)及び第10図(A)に示すよ
うに、光りが透過する対向する面が平面で且つ平行であ
るように構成されている。これにより光センサ−55の
悪用部全体に略均−に光が当たることとなり、測定結果
の安定性が向上する。
As shown in FIGS. 9(A) and 10(A), the inspection section 51 is configured such that opposing surfaces through which light passes are flat and parallel. As a result, the entire misused portion of the optical sensor 55 is illuminated with light approximately evenly, improving the stability of the measurement results.

第9図は検査部51を立方本形状としたもの、第10図
は送油管49を潰して対向面を平行とし、検査部51を
形成したものである。
FIG. 9 shows an inspection section 51 in the shape of a cubic book, and FIG. 10 shows an inspection section 51 formed by crushing the oil pipe 49 so that the opposing surfaces are parallel.

第11図及び第12図は遠心静電浄油機1の側面に取り
付けられたフック61の使用状態を示す全体斜視図及び
部分斜視図である。
11 and 12 are an overall perspective view and a partial perspective view showing how the hook 61 attached to the side surface of the centrifugal electrostatic oil purifier 1 is used.

第13図に示すように、フック61は遠心静電浄油機1
のケース3側面に係止ボルト65によって取り付けられ
ている。第15図に示す係止ボルト65は、一端にはネ
ジ部65cを形成し、他端のヘッド部分には係合六角部
65a及びその端辺に形成されたボルト段部65bとか
らなっている。また第14図に示すフック61はフラッ
トに形成された取付部6Toと半円弧状に湾曲された引
掛部61aとからなっており、取付部61bには係止ボ
ルト65が挿通する係止孔69が穿設されている。係止
孔69は引掛部61a側を円形に穿設した調節可動部7
3とし、引掛部61aの逆側には六角形に穿設した係止
部71としている。さらに係止孔69の周縁には段部6
9aが形成されている。
As shown in FIG. 13, the hook 61 is attached to the centrifugal electrostatic oil purifier 1.
It is attached to the side of the case 3 with a locking bolt 65. The locking bolt 65 shown in FIG. 15 has a threaded portion 65c formed at one end, an engaging hexagonal portion 65a at the head portion at the other end, and a bolt step portion 65b formed at the end thereof. . The hook 61 shown in FIG. 14 includes a flat mounting portion 6To and a hook portion 61a curved into a semicircular arc, and the mounting portion 61b has a locking hole 69 through which the locking bolt 65 is inserted. is drilled. The locking hole 69 is an adjustment movable part 7 that is circularly bored on the side of the hook part 61a.
3, and a hexagonal locking portion 71 is provided on the opposite side of the hook portion 61a. Further, a stepped portion 6 is provided at the periphery of the locking hole 69.
9a is formed.

第13図に示すように、停止ボルト65は外側からフッ
ク61及びケース3の側面を挿通し、ケース3の内側で
固定ナツト67と螺きすることによってフック61が締
着されている。またフック61とケース3側面の間には
ワッシャ68が介挿されている。ここで第1311及び
第16図に示すように、係止ボルト65の係き六角部6
5aはフック61の係止部71と係合するため、フック
61は回動不能に固定される。またフック61の向きを
変える場合には、第17121のように、フック61を
スライドさせて係止ボルト65を円形の調節可動部73
部分に位置せしめ、フック61を任意の方向へ向け、再
び係合六角部65aと1吊止部71を係合させる。また
係止孔69と係止ボルト65に設けられた段部69a 
、 65bは互いにti 合し、フック61が外側l\
抜は落ちないようになっている。
As shown in FIG. 13, the stop bolt 65 is inserted through the hook 61 and the side surface of the case 3 from the outside, and is screwed into the fixing nut 67 inside the case 3, thereby tightening the hook 61. Further, a washer 68 is inserted between the hook 61 and the side surface of the case 3. Here, as shown in FIG. 1311 and FIG.
5a engages with the locking portion 71 of the hook 61, so that the hook 61 is fixed unrotatably. In addition, when changing the direction of the hook 61, as shown in No. 17121, the hook 61 is slid and the locking bolt 65 is moved to the circular adjusting movable part 73.
the hook 61 in any direction, and the engaging hexagonal part 65a and the first hanging part 71 are engaged again. Also, a stepped portion 69a provided in the locking hole 69 and the locking bolt 65
, 65b are joined to each other, and the hook 61 is on the outside l\\
The nuki is designed not to fall.

以上のように遠心静電浄油機1のフック61収付構造を
設けることによって、フック61の用途が拡太し、第1
1図及び第12図に示すように、搬送移動時には吊りワ
イヤ62を引つtiけるための吊りフックとして、また
浄油作業場においては給油及び排油用のホース掛は等と
して利用することができる。
By providing the structure for housing the hook 61 of the centrifugal electrostatic oil purifier 1 as described above, the uses of the hook 61 are expanded, and the first
As shown in Figures 1 and 12, it can be used as a hanging hook for pulling the hanging wire 62 during transportation, and as a hose hook for refueling and draining oil in an oil purification workshop. .

〈発明の効果〉 以上の如く構成される本発明の装置において、特許請求
の範囲第1項記載の発明によれば、最下段近傍の孔が設
けられていない傘電極板によって、噴出口から出た浄化
すべき油が油槽底部のドレン系上方まで確実に案内され
るため、混入物がドレン系へ沈下しやすくなり1、従来
よりも浄化効率が向上するといった効果がある。
<Effects of the Invention> In the apparatus of the present invention configured as described above, according to the invention set forth in claim 1, the umbrella electrode plate near the bottom stage, which is not provided with holes, allows the air to flow out from the jet nozzle. Since the oil to be purified is reliably guided to the upper part of the drain system at the bottom of the oil tank, contaminants are more likely to sink into the drain system1, resulting in improved purification efficiency compared to the conventional method.

更に、特許請求の範囲第2項記載の発明によれば、最下
段の無孔全電極板部分で上記の如く混入物の分離促進と
ともに、遠心分離により浄化されて傾斜上方へ向かう油
を上方へ送り出すことによって更に浄油効率が上がると
いった効果も合わせ持つ。
Furthermore, according to the invention recited in claim 2, in addition to promoting the separation of contaminants as described above in the lowermost non-porous electrode plate portion, the oil that has been purified by centrifugation and is directed upward on the slope is directed upward. It also has the effect of further increasing oil purification efficiency by sending it out.

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

第1図は本発明の第一実施例の全体断面図、第2図は汚
染油を浄化する浄化回路系を示す全体図、第3図は最下
段傘電極板に案内されて流れる油と混入物の動きを示す
遠心静電浄油機の部分拡大断面図、第4図は傘電極板の
平面図、第5図は最下段傘電極板の平面図、第6図は第
二実施例の構造を示す遠心静電浄油機の部分拡大断面図
、第7図は第二実施例における最下段傘電極板の平面図
、第8図は同じくガイド部材の平面図、第9図<A)(
B)及び第10図(A)(B)は検査装置の構造を示す
平面図及び側面図、第11図はフックを取り付けた遠心
静電浄油機の全体斜視図、第12図はフックの他の用途
を示す部分斜視図、第13図はフックの取付状態を示す
部分拡大図、第14図はフックの全体正面図、第15図
は係止ボルトの側面全体図、第16図はフックの係止状
態における取付状態を示す正面図、第17図はフック調
節回動状態を示すフック正面図である。 1:遠心静電浄油機   5:油槽 19:軸         21:給油系23:傘電極
板     23a:孔
Fig. 1 is an overall cross-sectional view of the first embodiment of the present invention, Fig. 2 is an overall view showing a purification circuit system for purifying contaminated oil, and Fig. 3 is an overall view showing a purifying circuit system for purifying contaminated oil.Fig. A partial enlarged sectional view of the centrifugal electrostatic oil purifier showing the movement of objects, Fig. 4 is a plan view of the umbrella electrode plate, Fig. 5 is a plan view of the lowermost umbrella electrode plate, and Fig. 6 is a diagram of the second embodiment. FIG. 7 is a plan view of the lowermost umbrella electrode plate in the second embodiment; FIG. 8 is a plan view of the guide member; FIG. 9 <A) (
B) and Figures 10 (A) and (B) are a plan view and side view showing the structure of the inspection device, Figure 11 is an overall perspective view of a centrifugal electrostatic oil purifier with a hook attached, and Figure 12 is a diagram showing the structure of the hook. Fig. 13 is a partially enlarged view showing the hook installed, Fig. 14 is an overall front view of the hook, Fig. 15 is an overall side view of the locking bolt, and Fig. 16 is a partial perspective view of the hook. FIG. 17 is a front view of the hook showing the hook adjustment rotation state. 1: Centrifugal electrostatic oil purifier 5: Oil tank 19: Shaft 21: Oil supply system 23: Umbrella electrode plate 23a: Hole

Claims (1)

【特許請求の範囲】 1)回転油槽(5)内に設けられた軸(19)と、該軸
(19)に所定間隔で積層設置され孔(23a)が穿設
された複数の傘電極板(23)と、前記回転油槽(5)
内側壁面に設けられた前記傘電極板(23)と異極とな
る電極(31)と、最下段の傘電極板(25)下側に設
けられた浄化すべき油を噴出する噴出口(27)とによ
って、回転油槽(5)の底部近傍噴出口(27)から浄
化すべき油を上方へ流動させる給排油系(21)、(3
3)を構成し、前記給排油系(21)、(33)の下側
には混入物を滞留排出するドレン系(35)を設けた構
造において、最下段近傍の傘電極板(25)を無孔とし
た遠心静電浄油機。 2)該最下段傘電極板(37)と噴出口(27)との間
には噴出した浄化すべき油の上方流動を規制するガイド
部材(39)を設け、該ガイド部材(39)の周縁が対
向する部位より下方の上記最下段傘電極板(37)を無
孔とし、前記ガイド部材(39)の周縁が対向する部位
より上方の上記最下段傘電極板(37)に孔(37a)
を穿設した特許請求の範囲第1項記載の遠心静電浄油機
[Claims] 1) A shaft (19) provided in the rotary oil tank (5), and a plurality of umbrella electrode plates stacked on the shaft (19) at predetermined intervals and having holes (23a) formed therein. (23) and the rotary oil tank (5)
An electrode (31) having a different polarity from the umbrella electrode plate (23) provided on the inner wall surface, and a spout (27) for spouting oil to be purified provided below the umbrella electrode plate (25) at the lowest stage. ), the oil supply and drainage system (21), (3
3), and a drain system (35) for retaining and discharging contaminants is provided below the oil supply and drainage systems (21) and (33), and the umbrella electrode plate (25) near the bottom stage A non-porous centrifugal electrostatic oil purifier. 2) A guide member (39) is provided between the lowermost umbrella electrode plate (37) and the spout (27) for regulating the upward flow of the oil to be purified that has spouted out, and the periphery of the guide member (39) The lowermost umbrella electrode plate (37) below the area facing the guide member (39) is made non-porous, and the lowermost umbrella electrode plate (37) above the area facing the peripheral edge of the guide member (39) has holes (37a).
A centrifugal electrostatic oil purifier according to claim 1, wherein the centrifugal electrostatic oil purifier is provided with:
JP63231316A 1988-09-14 1988-09-14 Centrifugal electrostatic oil cleaner Pending JPH0278454A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63231316A JPH0278454A (en) 1988-09-14 1988-09-14 Centrifugal electrostatic oil cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63231316A JPH0278454A (en) 1988-09-14 1988-09-14 Centrifugal electrostatic oil cleaner

Publications (1)

Publication Number Publication Date
JPH0278454A true JPH0278454A (en) 1990-03-19

Family

ID=16921724

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63231316A Pending JPH0278454A (en) 1988-09-14 1988-09-14 Centrifugal electrostatic oil cleaner

Country Status (1)

Country Link
JP (1) JPH0278454A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008501505A (en) * 2004-06-03 2008-01-24 アルファ ラヴァル コーポレイト アクチボラゲット Apparatus and method for purifying gas
EP1907124A1 (en) * 2005-06-27 2008-04-09 3Nine AB Method and apparatus for separation of particles from a flow of gas
KR20180047967A (en) * 2016-11-02 2018-05-10 씨에이티 주식회사 a seperator oil mist and moisture for COG
KR20190010676A (en) * 2019-01-11 2019-01-30 씨에이티 주식회사 Oil mist seperator
WO2019081469A1 (en) * 2017-10-26 2019-05-02 Gea Mechanical Equipment Gmbh Method for processing a flowable product and centrifuge

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008501505A (en) * 2004-06-03 2008-01-24 アルファ ラヴァル コーポレイト アクチボラゲット Apparatus and method for purifying gas
US7704300B2 (en) 2004-06-03 2010-04-27 Alfa Laval Corporate Ab Device and a method for cleaning of a gas
JP4885127B2 (en) * 2004-06-03 2012-02-29 アルファ ラヴァル コーポレイト アクチボラゲット Apparatus and method for purifying gas
EP1907124A1 (en) * 2005-06-27 2008-04-09 3Nine AB Method and apparatus for separation of particles from a flow of gas
EP1907124A4 (en) * 2005-06-27 2011-03-30 3Nine Ab Method and apparatus for separation of particles from a flow of gas
US8029601B2 (en) 2005-06-27 2011-10-04 3Nine Ab Method and apparatus for separation of particles from a flow of gas
KR20180047967A (en) * 2016-11-02 2018-05-10 씨에이티 주식회사 a seperator oil mist and moisture for COG
WO2019081469A1 (en) * 2017-10-26 2019-05-02 Gea Mechanical Equipment Gmbh Method for processing a flowable product and centrifuge
US11660612B2 (en) 2017-10-26 2023-05-30 Gea Mechanical Equipment Gmbh Method for processing a flowable product by electrically charging particles in the flowable product and a disc stack of a centrifuge
KR20190010676A (en) * 2019-01-11 2019-01-30 씨에이티 주식회사 Oil mist seperator

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