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JPS6242764Y2 - - Google Patents

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Publication number
JPS6242764Y2
JPS6242764Y2 JP10857081U JP10857081U JPS6242764Y2 JP S6242764 Y2 JPS6242764 Y2 JP S6242764Y2 JP 10857081 U JP10857081 U JP 10857081U JP 10857081 U JP10857081 U JP 10857081U JP S6242764 Y2 JPS6242764 Y2 JP S6242764Y2
Authority
JP
Japan
Prior art keywords
flow rate
viscosity
liquid
oil
purification
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
JP10857081U
Other languages
Japanese (ja)
Other versions
JPS5814954U (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 JP10857081U priority Critical patent/JPS5814954U/en
Publication of JPS5814954U publication Critical patent/JPS5814954U/en
Application granted granted Critical
Publication of JPS6242764Y2 publication Critical patent/JPS6242764Y2/ja
Granted legal-status Critical Current

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  • Electrostatic Separation (AREA)
  • Control Of Non-Electrical Variables (AREA)

Description

【考案の詳細な説明】 本考案は、油等の絶縁性液体を静電的に浄化す
る液体浄化装置に関し、特に、粘度変化に対応し
て浄化効率を高めるように改良した浄化装置に関
するものである。
[Detailed description of the invention] The present invention relates to a liquid purification device that electrostatically purifies insulating liquids such as oil, and in particular to a purification device that has been improved to increase purification efficiency in response to viscosity changes. be.

従来のこの種の装置は、第1図に示したように
構成されている。第1図において、1は液体浄化
装置本体で、内部に正電極2および負電極3を交
互に配置し、その電極間に集塵体4を設けてい
る。5は高圧電源で、前記正電極2と負電極3と
の間に10kV程度の高電圧を供給する。また、被
浄化液体を導入するためのポンプ6とバルブ7を
備えており、タンク8内の被浄化液体を、ホース
9を通して本体下部から導入し、前記集塵体4を
通過させて本体上部からホース10を通してタン
ク8へ戻すように循環させて浄化する。
A conventional device of this type is constructed as shown in FIG. In FIG. 1, reference numeral 1 denotes a main body of a liquid purification device, in which positive electrodes 2 and negative electrodes 3 are arranged alternately, and a dust collector 4 is provided between the electrodes. Reference numeral 5 denotes a high voltage power supply, which supplies a high voltage of about 10 kV between the positive electrode 2 and the negative electrode 3. It is also equipped with a pump 6 and a valve 7 for introducing the liquid to be purified, and the liquid to be purified in the tank 8 is introduced from the lower part of the main body through a hose 9, passed through the dust collector 4, and then from the upper part of the main body. The water is circulated through the hose 10 and returned to the tank 8 for purification.

ところが、この装置の浄液能力を仮に、単位時
間当りに一定汚染度から一定の浄化を行う液量で
表わすと、第2図に示したように、液の粘度が高
くなるに従つて浄液能力が低下する。これを具体
例で示すと、例えば、同じ装置を使つて異なる粘
度の油を浄化し比較すると、粘度の高い油は低い
油に比べて浄油能力が極端に低く、利用者にとま
どいを与える可能性があつた。さらに、同じ油で
あつても、油温が変われば粘度も大きく変化する
ため、例えば成形機の作動油等の場合で、40℃前
後の油はそのまま浄化する場合と、20℃程度の常
温で浄化する場合とでは、後者の方が粘度がかな
り高いため、浄油能力が数分の1となり、浄化処
理量が減少してしまうという欠点があつた。
However, if the liquid purification capacity of this device is expressed as the amount of liquid that purifies a certain degree of contamination per unit time, as shown in Figure 2, as the viscosity of the liquid increases, the purification capacity increases. Capacity decreases. To give a concrete example of this, for example, if you use the same equipment to purify and compare oils with different viscosities, the oil with a higher viscosity will have an extremely lower oil purification ability than the oil with a lower viscosity, which may cause confusion to the user. The sex was hot. Furthermore, even if the oil is the same, the viscosity will change greatly if the oil temperature changes, so for example, in the case of hydraulic oil for a molding machine, oil at around 40°C can be purified as is, and oil at room temperature around 20°C can be purified. Compared to the case of purification, the latter has a considerably higher viscosity, so the oil purification capacity is reduced to a fraction of that, resulting in a reduction in the amount of purification.

また、低粘度の油は一般に切削油や放電加工油
等のように金属微粉などを多量に含んだものが多
く、浄油能力がかえつて高過ぎて集塵体4の入口
付近に集中して集塵されるため、その塵埃により
正、負電極間の絶縁抵抗が低下し、電流が多く流
れ過ぎて電圧が低下するので静電集塵ができなく
なつたり、集塵体4の寿命が短かくなる等の欠点
もあつた。
In addition, low-viscosity oils generally contain a large amount of metal fine particles, such as cutting oils and electrical discharge machining oils, and their oil purification ability is rather high, concentrating near the entrance of the dust collector 4. As the dust is collected, the insulation resistance between the positive and negative electrodes decreases, causing too much current to flow and lowering the voltage, which may make electrostatic dust collection impossible or shorten the life of the dust collector 4. There were also drawbacks such as being dark.

本考案は、上記従来例の欠点を解消するため
に、被浄化液体の粘度が高いときは流量を自動的
に減少させて浄化能力を高め、また粘度が低いと
きは流量を増加させて集塵体の寿命を延ばすよう
にした液体浄化装置を提供するものである。以
下、図面により実施例を詳細に説明する。
In order to eliminate the drawbacks of the conventional example, the present invention automatically reduces the flow rate when the viscosity of the liquid to be purified is high to increase the purification ability, and increases the flow rate when the viscosity is low to collect dust. To provide a liquid purification device designed to extend the lifespan of the body. Hereinafter, embodiments will be described in detail with reference to the drawings.

第3図は、本考案の一実施例を示したもので、
第1図と同一符号のものは同一のものを示してお
り、11は浄化装置本体1の液送出口に設けた流
量制御管である。この流量制御管11は第4図に
示したように、内部に複数本の細管12を束にし
て装填したもので、ここを流れる液体の粘度によ
つて圧力損失が変つてくる。即ち、液体の粘度が
高い程、流量制御管11の圧力損失が増加し、従
つて流量が減少する。逆に、液体の粘度が低い
程、圧力損失が低下し、流量が増加する。
FIG. 3 shows an embodiment of the present invention.
The same reference numerals as in FIG. 1 indicate the same parts, and 11 is a flow rate control pipe provided at the liquid delivery port of the purifier main body 1. As shown in FIG. 4, this flow rate control tube 11 has a plurality of thin tubes 12 loaded inside it in a bundle, and the pressure loss changes depending on the viscosity of the liquid flowing therethrough. That is, the higher the viscosity of the liquid, the greater the pressure loss in the flow control tube 11, and therefore the lower the flow rate. Conversely, the lower the viscosity of the liquid, the lower the pressure drop and the higher the flow rate.

ここで、浄化装置を流れる液体の流量と浄化能
力との関係を第5図に示すと、曲線Aは比較的低
粘度の油の場合、曲線Bは比較的高粘度の油の場
合、曲線Cは、AとBの中間の粘度の油の場合で
ある。この図から明らかなように、同一流量の場
合は、第2図においても説明したように、高粘度
の油(曲線B)ほど浄化能力は低いが、流量制御
管11を設けて粘度が高い程流量を少なくすれ
ば、浄化能力を高めることができる。一方、低粘
度の油(曲線A)で、切削屑等の塵埃が多く含ま
れているものでは、流量制御管11の圧力損失も
低いから流量は多く、従つて浄化能力は低下し、
集塵体4の入口付近で集中して集塵することな
く、集塵体4の全体で略均一に集塵することにな
るから、集塵体4の寿命を延ばすことができる。
Here, when the relationship between the flow rate of liquid flowing through the purification device and the purification capacity is shown in Fig. 5, curve A is for relatively low viscosity oil, curve B is for relatively high viscosity oil, and curve C is for relatively high viscosity oil. is for an oil with a viscosity between A and B. As is clear from this figure, when the flow rate is the same, as explained in Fig. 2, the higher the viscosity of the oil (curve B), the lower the purification ability. Purification ability can be increased by reducing the flow rate. On the other hand, if the oil has a low viscosity (curve A) and contains a lot of dust such as cutting chips, the pressure loss in the flow control pipe 11 is low, so the flow rate is high, and the purification ability is reduced.
Since the dust is not concentrated near the entrance of the dust collector 4 and the dust is collected substantially uniformly throughout the dust collector 4, the life of the dust collector 4 can be extended.

なお、流量が少なくなると浄化能力が上がる理
由は、液体中の塵埃が電極間の静電界により集塵
体4に吸引される滞留時間が長くなり、従つて塵
埃が集塵体間を通過する間に吸着する確率が高く
なるためである。
The reason why the purification ability increases as the flow rate decreases is that the residence time for dust in the liquid to be sucked into the dust collector 4 by the electrostatic field between the electrodes becomes longer, and therefore the time required for the dust to pass between the dust collectors becomes longer. This is because the probability of adsorption to is increased.

なお、本実施例における流量制御管11の代り
に、粘度検知器と、この検知器に連動して流量を
制御するポンプを設けても同様の効果を得ること
ができる。
Note that the same effect can be obtained by providing a viscosity detector and a pump that controls the flow rate in conjunction with this detector in place of the flow rate control pipe 11 in this embodiment.

以上説明したように、本考案によれば、被浄化
液体の粘度の高、低に対応して浄化装置内を流れ
る液体の流量を減、増することにより、粘度が高
くても浄化能力を確保し、また逆に、粘度が低く
一般に切削屑等を多く含むものに対しては浄化能
力を適当に落すことにより、集塵体が平均して集
塵するようにして静電効果を持続させ、集塵体の
寿命を延ばすことができるなど、大きな効果を有
するものである。
As explained above, according to the present invention, by reducing or increasing the flow rate of the liquid flowing through the purification device in response to the high or low viscosity of the liquid to be purified, purification ability is ensured even when the viscosity is high. On the other hand, for materials with low viscosity and generally containing a lot of cutting waste, the purification ability is appropriately reduced so that the dust collector collects the dust evenly and the electrostatic effect is maintained. This has great effects such as being able to extend the life of the dust collector.

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

第1図は、従来例の構成図、第2図は、従来例
による被浄化液の粘度と浄液能力との関係を示す
図、第3図は、本考案の一実施例の構成図、第4
図は、流量制御管の内部構成を示す図、第5図
は、粘度の異なる被浄化液体の流量と浄化能力と
の関係を示す図である。 2……正電極、3……負電極、4……集塵体、
5……高圧電源、6……ポンプ、8……タンク、
11……流量制御管、12……細管。
FIG. 1 is a configuration diagram of a conventional example, FIG. 2 is a diagram showing the relationship between the viscosity of a liquid to be purified and liquid purification ability according to a conventional example, and FIG. 3 is a configuration diagram of an embodiment of the present invention. Fourth
This figure shows the internal structure of the flow rate control pipe, and FIG. 5 is a diagram showing the relationship between the flow rate and purification capacity of liquids to be purified having different viscosities. 2... Positive electrode, 3... Negative electrode, 4... Dust collector,
5...High voltage power supply, 6...Pump, 8...Tank,
11...flow control tube, 12... thin tube.

Claims (1)

【実用新案登録請求の範囲】 (1) 内部に静電浄化手段を備え、油等の絶縁性液
体を通過させて浄化する装置において、前記絶
縁性液体の粘度が高いときは通過流量を少なく
し、粘度が低いときは通過流量を多くする流量
制御手段を装置からの流出路に設けたことを特
徴とする液体浄化装置。 (2) 前記流量制御手段は、前記絶縁性液体の粘度
を検知する検知器と、この検知結果により流量
を制御するポンプとからなることを特徴とする
実用新案登録請求の範囲第(1)項記載の液体浄化
装置。 (3) 前記流量制御手段は、複数の細管を束ねて内
蔵し、前記絶縁性液体の流通路の一区画を構成
する流量制御管からなることを特徴とする実用
新案登録請求の範囲第(1)項記載の液体浄化装
置。
[Claims for Utility Model Registration] (1) In a device that has an electrostatic purification means inside and purifies an insulating liquid such as oil by passing it through, when the viscosity of the insulating liquid is high, the passing flow rate is reduced. A liquid purification device characterized in that a flow rate control means for increasing the flow rate when the viscosity is low is provided in the outflow path from the device. (2) Utility model registration claim (1), characterized in that the flow rate control means comprises a detector that detects the viscosity of the insulating liquid, and a pump that controls the flow rate based on the detection result. Liquid purification device as described. (3) The flow rate control means is comprised of a flow rate control tube that includes a plurality of thin tubes bundled together and constitutes one section of the flow path for the insulating liquid. ) The liquid purification device described in item ).
JP10857081U 1981-07-23 1981-07-23 liquid purification device Granted JPS5814954U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10857081U JPS5814954U (en) 1981-07-23 1981-07-23 liquid purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10857081U JPS5814954U (en) 1981-07-23 1981-07-23 liquid purification device

Publications (2)

Publication Number Publication Date
JPS5814954U JPS5814954U (en) 1983-01-29
JPS6242764Y2 true JPS6242764Y2 (en) 1987-11-02

Family

ID=29902972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10857081U Granted JPS5814954U (en) 1981-07-23 1981-07-23 liquid purification device

Country Status (1)

Country Link
JP (1) JPS5814954U (en)

Also Published As

Publication number Publication date
JPS5814954U (en) 1983-01-29

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