JPH0317991Y2 - - Google Patents

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Publication number
JPH0317991Y2
JPH0317991Y2 JP10470287U JP10470287U JPH0317991Y2 JP H0317991 Y2 JPH0317991 Y2 JP H0317991Y2 JP 10470287 U JP10470287 U JP 10470287U JP 10470287 U JP10470287 U JP 10470287U JP H0317991 Y2 JPH0317991 Y2 JP H0317991Y2
Authority
JP
Japan
Prior art keywords
cyclone
tank
solvent
cleaning tank
ultrasonic cleaning
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
Application number
JP10470287U
Other languages
Japanese (ja)
Other versions
JPS63164988U (en
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 filed Critical
Priority to JP10470287U priority Critical patent/JPH0317991Y2/ja
Publication of JPS63164988U publication Critical patent/JPS63164988U/ja
Application granted granted Critical
Publication of JPH0317991Y2 publication Critical patent/JPH0317991Y2/ja
Expired legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Cyclones (AREA)

Description

【考案の詳細な説明】 本考案は液を循環させる方式の洗浄システムに
関するもので、特にサイクロンと沈殿槽とによつ
て液を清浄化する場合の効率を向上させるもので
ある。
[Detailed Description of the Invention] The present invention relates to a cleaning system that circulates liquid, and in particular improves efficiency when cleaning liquid using a cyclone and a sedimentation tank.

機械部分は長時間の使用後、摩耗や外部から入
り込んだスラツジによつて汚れを生じ、スラツジ
中の鉄粉や砂によつて部品の動作に円滑さを失な
い、その部品の機能を果さなくしている。
After long-term use, mechanical parts become dirty due to wear and sludge that has entered from outside, and iron powder and sand in the sludge prevent parts from operating smoothly and prevent the parts from performing their functions. I've lost it.

従来、これらスラツジは超音波洗浄機等で除去
しているが、除去されたスラツジは今度は溶剤を
汚すことになる。したがつて溶剤をフイルター等
によつてろ過することも行なわれているが、フイ
ルタの目詰りが頻発する。又蒸留法は大量の熱エ
ネルギーを必要とするので実用的でなく、遠心分
離法もかなりの動力を要し省エネルギー対策上好
ましくはない。
Conventionally, these sludges have been removed using an ultrasonic cleaner or the like, but the removed sludges then contaminate the solvent. Therefore, although it has been attempted to filter the solvent using a filter or the like, the filter often becomes clogged. In addition, the distillation method requires a large amount of thermal energy and is therefore impractical, and the centrifugation method also requires a considerable amount of power and is not preferred from the viewpoint of energy conservation.

本考案は遠心分離機の数分の1の動力で溶剤の
回収が可能な装置を提供するものである。
The present invention provides an apparatus that can recover solvent with a fraction of the power of a centrifugal separator.

以下図によりこれを説明する。 This will be explained below with reference to the drawings.

図において、1は超音波洗浄槽であつて被洗浄
部品2,2,2がかご3に収納されてローラチエ
ーン装置4で搬入される。5は槽内に入れられた
石油系溶剤である。6は槽底に取付けられた超音
波振動子であつて、発振器(図示せず)で駆動さ
れる。7は凡用されているサイクロンであつてそ
の流入口には超音波洗浄槽1の汚れた溶剤がポン
プ8で送り込まれる。Tはタイマーであつてポン
プ8を5分毎に0.5分程度駆動する。9は圧力計
である。サイクロン下部の流出口10はバンカー
11に通じている。12はバンカーの下部取出弁
である。13は沈澱槽であつて、バンカー11の
小出用弁14から溶剤5の一部が取込まれる他サ
イクロン7の内筒15からの清浄液に含まれる粒
子径の微小なものが側路弁16によつて取込まれ
る。17は沈澱物の取出口用弁である。18は沈
澱槽13の上層液を超音波洗浄槽へ送入する移送
弁である。洗浄槽1にはサイクロン7の内筒から
の清浄液も送り込まれる。
In the figure, reference numeral 1 denotes an ultrasonic cleaning tank, in which parts to be cleaned 2, 2, 2 are stored in a basket 3 and transported by a roller chain device 4. 5 is a petroleum solvent placed in the tank. Reference numeral 6 denotes an ultrasonic vibrator attached to the bottom of the tank, which is driven by an oscillator (not shown). Reference numeral 7 denotes a commonly used cyclone, into which the dirty solvent from the ultrasonic cleaning tank 1 is fed by a pump 8. T is a timer that drives the pump 8 for about 0.5 minutes every 5 minutes. 9 is a pressure gauge. An outlet 10 at the bottom of the cyclone communicates with a bunker 11. 12 is a lower bunker take-out valve. Reference numeral 13 is a sedimentation tank, into which part of the solvent 5 is taken in from the dispensing valve 14 of the bunker 11, and small particles contained in the cleaning liquid from the inner cylinder 15 of the cyclone 7 are collected through a side passage valve. 16. 17 is a valve for taking out the sediment. 18 is a transfer valve that sends the upper layer liquid of the settling tank 13 to the ultrasonic cleaning tank. Cleaning liquid from the inner cylinder of the cyclone 7 is also sent into the cleaning tank 1.

サイクロン装置の内筒15から送出される溶剤
は、パイプにより超音波洗浄槽1に給送される。
サイクロン装置の内筒15から送出される溶剤の
一部は、上記パイプから分岐するパイプにより沈
殿槽13に給送される。このパイプには、流量を
調節するため、側路弁16が取り付けられてい
る。
The solvent sent out from the inner cylinder 15 of the cyclone device is fed to the ultrasonic cleaning tank 1 through a pipe.
A part of the solvent sent out from the inner cylinder 15 of the cyclone device is fed to the settling tank 13 by a pipe branching from the above-mentioned pipe. A side valve 16 is attached to this pipe to adjust the flow rate.

上記装置において、超音波洗浄により部品の鉄
粉や砂で汚れた洗浄槽中の溶剤はポンプ8により
サイクロン7に送られる。溶剤はサイクロン中で
遠心力を与えられて比重の大きいスラツジがサイ
クロン内壁を下方へ沈降してバンカー内に送り込
まれる。サイクロン下部で上部方向に圧力を受け
た比重の小さい清浄液は上昇流となつてサイクロ
ン内筒15から外部へ噴出され超音波洗浄槽へ移
される。この循環系は約5分程続けられ、この間
洗浄槽1内には噴流が生じて、超音波洗浄では落
ち難い泥等の汚れを落す。
In the above apparatus, the solvent in the cleaning tank contaminated with iron powder and sand from parts due to ultrasonic cleaning is sent to the cyclone 7 by the pump 8. The solvent is subjected to centrifugal force in the cyclone, and the sludge with a high specific gravity settles down the inner wall of the cyclone and is sent into the bunker. The cleaning liquid, which has a low specific gravity and is subjected to upward pressure at the lower part of the cyclone, becomes an upward flow and is ejected from the cyclone inner cylinder 15 to the outside and transferred to the ultrasonic cleaning tank. This circulation system continues for about 5 minutes, during which time a jet stream is generated in the cleaning tank 1 to remove dirt such as mud that is difficult to remove with ultrasonic cleaning.

ところで、サイクロンにより分離できるスラツ
ジの粒径には限界がある。
However, there is a limit to the particle size of sludge that can be separated by a cyclone.

すなわち、分離限果粒子dsは、 g:重力加速度 9.8m/s2 u:液体の粘度 rs:スラツジの比重量 ψ0:サイクロン入口での流速 r1:サイクロンの内半径 r2:サイクロン内筒半径 hi:バンカー上端から内筒下端までの高さ r0:サイクロン入口の内半径 となり、サイクロンの各部機械寸法によつて決ま
る。限界粒径を下げると損失抵抗が増大するた
め、サイクロン自体の粒径はある程度以下に出来
ない。本考案は、洗浄槽を活用することによりこ
れを解決するものである。
That is, the separated limiting particle ds is g: Gravitational acceleration 9.8m/s 2 u: Viscosity of liquid rs: Specific weight of sludge ψ 0 : Flow velocity at cyclone inlet r 1 : Inner radius of cyclone r 2 : Radius of cyclone inner cylinder hi: From upper end of bunker to lower end of inner cylinder Height r 0 : This is the inner radius of the cyclone inlet and is determined by the machine dimensions of each part of the cyclone. If the critical particle size is lowered, loss resistance increases, so the particle size of the cyclone itself cannot be reduced below a certain level. The present invention solves this problem by utilizing a cleaning tank.

本考案ではサイクロンから沈澱槽13への通路
は、通常のバンカー上部に設けた小出口からとサ
イクロン内筒により取出した溶剤の一部を側路さ
せるものと2種類設けている。弁14と弁16と
がそれである。このようにすると、側路弁16か
らはサイクロン7の分離限界粒径以下の微少なス
ラツジを含んだ液が沈澱槽へ流入し、小出口弁1
4からはサイクロンの分離限界粒径以上のスラツ
ジを含む液が沈澱槽へ流入する。しかも、小出口
弁14から液を噴出させることによつて、サイク
ロン内のスラツジの沈降速度を増大し、分離効果
を高めることが出来る。
In the present invention, two types of passages are provided from the cyclone to the settling tank 13: one is a small outlet provided at the top of a normal bunker, and the other is a passage through which a portion of the solvent taken out by the cyclone inner cylinder is bypassed. These include valves 14 and 16. In this way, the liquid containing minute sludge with a particle diameter below the separation limit of the cyclone 7 flows from the side valve 16 into the settling tank, and the small outlet valve 1
From No. 4, a liquid containing sludge with a particle size larger than the separation limit of the cyclone flows into the settling tank. Moreover, by spouting the liquid from the small outlet valve 14, the sedimentation speed of the sludge in the cyclone can be increased and the separation effect can be enhanced.

なお、沈澱槽13内の上澄液は弁18を通して
洗浄槽1へ戻される。
Note that the supernatant liquid in the settling tank 13 is returned to the cleaning tank 1 through the valve 18.

なお、ポンプ8によつて洗浄槽1の液をサイク
ロン7に移す場合、サイクロン側の許容流入量を
超えた分は超音波洗浄槽1に戻すための側路19
を設けてもよい。
Note that when the liquid in the cleaning tank 1 is transferred to the cyclone 7 by the pump 8, the amount exceeding the allowable inflow amount on the cyclone side is returned to the ultrasonic cleaning tank 1 through a side channel 19.
may be provided.

以上説明したように、本考案によれば、側路弁
16により微少なスラツジをも沈澱槽で除去でき
る他、清水状態で効率良く超音波洗浄槽を行なう
一方、間欠的に、洗浄槽内に噴流を起して、超音
波洗浄では落ち難い汚れを機械的に落して種々の
汚れに対して清浄効率を高め且つサイクロンや沈
澱槽の働きによつて、溶剤中のスラツジが除去さ
れ常に清浄な液中で効率の良い洗浄が行なわれる
利点がある。
As explained above, according to the present invention, even the smallest amount of sludge can be removed in the sedimentation tank by the bypass valve 16, and while the ultrasonic cleaning tank can be efficiently carried out in fresh water state, the cleaning tank is intermittently A jet stream is generated to mechanically remove dirt that is difficult to remove with ultrasonic cleaning, increasing the cleaning efficiency for various types of dirt, and the cyclone and sedimentation tank remove sludge in the solvent to ensure cleanliness at all times. This has the advantage that efficient cleaning can be carried out in liquid.

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

図は本案装置の系統図である。 1……超音波洗浄槽、2……被洗浄物、6……
超音波振動子、7……サイクロン、9……圧力
計、11……バンカー、13……洗澱槽、14…
…小出口用弁、16……側路弁。
The figure is a system diagram of the proposed device. 1...Ultrasonic cleaning tank, 2...Object to be cleaned, 6...
Ultrasonic vibrator, 7...Cyclone, 9...Pressure gauge, 11...Bunker, 13...Washing tank, 14...
...Small outlet valve, 16... Side passage valve.

Claims (1)

【実用新案登録請求の範囲】 超音波洗浄槽と、 超音波洗浄槽の汚れた溶剤が供給されるサイク
ロン装置と、 サイクロン装置の内筒から送出される溶剤を上
記超音波洗浄槽に給送するパイプと、 上記サイクロン装置のバンカーから送出される
溶剤が供給される沈殿槽と、 上記沈殿槽の上澄液を上記超音波洗浄槽に給送
する手段と、 上記サイクロン装置の内筒から送出される溶剤
の一部を上記沈殿槽に給送する上記パイプから分
岐するパイプとを有して成る超音波洗浄装置。
[Scope of claim for utility model registration] An ultrasonic cleaning tank, a cyclone device to which dirty solvent from the ultrasonic cleaning tank is supplied, and a solvent sent from the inner cylinder of the cyclone device to the ultrasonic cleaning tank. a pipe; a settling tank to which the solvent sent out from the bunker of the cyclone device is supplied; a means for feeding the supernatant liquid of the settling tank to the ultrasonic cleaning tank; and a pipe branching from the pipe for feeding a part of the solvent to the precipitation tank.
JP10470287U 1987-07-08 1987-07-08 Expired JPH0317991Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10470287U JPH0317991Y2 (en) 1987-07-08 1987-07-08

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10470287U JPH0317991Y2 (en) 1987-07-08 1987-07-08

Publications (2)

Publication Number Publication Date
JPS63164988U JPS63164988U (en) 1988-10-27
JPH0317991Y2 true JPH0317991Y2 (en) 1991-04-16

Family

ID=30978443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10470287U Expired JPH0317991Y2 (en) 1987-07-08 1987-07-08

Country Status (1)

Country Link
JP (1) JPH0317991Y2 (en)

Also Published As

Publication number Publication date
JPS63164988U (en) 1988-10-27

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