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JPH0134730B2 - - Google Patents
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JPH0134730B2 - - Google Patents

Info

Publication number
JPH0134730B2
JPH0134730B2 JP55070674A JP7067480A JPH0134730B2 JP H0134730 B2 JPH0134730 B2 JP H0134730B2 JP 55070674 A JP55070674 A JP 55070674A JP 7067480 A JP7067480 A JP 7067480A JP H0134730 B2 JPH0134730 B2 JP H0134730B2
Authority
JP
Japan
Prior art keywords
machining
tank
fluid
machining fluid
activated carbon
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
JP55070674A
Other languages
Japanese (ja)
Other versions
JPS571619A (en
Inventor
Shigeo Yamada
Toshiro Ooizumi
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 Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP7067480A priority Critical patent/JPS571619A/en
Publication of JPS571619A publication Critical patent/JPS571619A/en
Publication of JPH0134730B2 publication Critical patent/JPH0134730B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23HWORKING OF METAL BY THE ACTION OF A HIGH CONCENTRATION OF ELECTRIC CURRENT ON A WORKPIECE USING AN ELECTRODE WHICH TAKES THE PLACE OF A TOOL; SUCH WORKING COMBINED WITH OTHER FORMS OF WORKING OF METAL
    • B23H1/00Electrical discharge machining, i.e. removing metal with a series of rapidly recurring electrical discharges between an electrode and a workpiece in the presence of a fluid dielectric
    • B23H1/10Supply or regeneration of working media

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physical Water Treatments (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Description

【発明の詳細な説明】 本発明は放電加工装置、特に有機化合物を燃焼
しない割合で水に混合した加工液中で、被加工物
に放電加工を施す放電加工装置の改良に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an electric discharge machining apparatus, particularly an electric discharge machining apparatus that performs electric discharge machining on a workpiece in a machining liquid containing an organic compound mixed with water at a proportion that does not burn it.

一般に、加工液を用いる放電加工装置は、加工
液の比抵抗値を一定値以上に保つて用いる必要
上、イオン交換樹脂による比抵抗値向上が行なわ
れていた。ところが、イオン交換樹脂には、放電
加工によつて生じたスラツジが吸着し易く、これ
が為その寿命を著しく低下させることが知られて
いる。そこで、2μ以上のスラツジ除去の為に、
紙、布等から成るフイルターを設け、2μ以下の
スラツジ除去の為に、活性炭濾過槽を用いること
について先に提案した。
In general, electric discharge machining equipment that uses machining fluid has been used to maintain the specific resistance value of the machining fluid above a certain value, so ion exchange resins have been used to improve the resistivity value. However, it is known that ion exchange resins tend to adsorb sludge generated by electrical discharge machining, which significantly shortens their lifespan. Therefore, in order to remove sludge of 2μ or more,
Previously, we proposed using an activated carbon filtration tank with a filter made of paper, cloth, etc., to remove sludge of 2μ or less.

この装置は、第1図に示す様な、水と有機化合
物との溶液から成る加工液10中で放電加工を行
なう加工槽12と、加工槽12中の加工液10の
スラツジ除去を行なうフイルター14、活性炭濾
過槽16及び、加工液10の比抵抗値を向上させ
るイオン交換槽18とをその途中に配し、加工液
10を循環させる加工液循環装置20とから成
る。加工槽12の加工液10中には、電極22と
被加工物24とを対峙して位置させてある。加工
液循環装置20は、加工槽12で放電加工を行な
つてスラツジを含んだ加工液10を送入する排液
槽26と、加工槽12に加工液10を供給する供
給液槽28とを有している。排液槽26中の加工
液10は、圧力ポンプ30で、紙、布等を用いた
フイルター14に送られた後、分流されて一部が
供給液槽28に送られる。分流されて供給液槽2
8に送られた残りは、電磁バルブ32を途中に介
して、順次活性炭濾過槽16、イオン交換槽18
へと送られた後、同様に供給液槽28に送られ
る。供給液槽28中の加工液10は、圧力ポンプ
34で加工槽12に送られつつ、一部を分流させ
て比抵抗測定器36を通して、比抵抗値を測定す
る。図中38は、比抵抗測定器36で測定した比
抵抗値によつて、電磁バルブ32を開閉し、イオ
ン交換槽18に送る加工液10流量の調整を行な
うコントロールボツクスである。又、図中40,
42は、各々加工液10の流量を調整するバルブ
である。更に、活性炭濾過槽16と、イオン交換
槽18との間には、目視判定用の濾過判定器44
が設けてある。
This apparatus, as shown in FIG. 1, includes a machining tank 12 in which electrical discharge machining is performed in a machining fluid 10 made of a solution of water and an organic compound, and a filter 14 that removes sludge from the machining fluid 10 in the machining tank 12. , an activated carbon filtration tank 16, and an ion exchange tank 18 for improving the specific resistance value of the machining fluid 10, which is disposed in the middle thereof, and a machining fluid circulation device 20 that circulates the machining fluid 10. In the machining fluid 10 of the machining tank 12, an electrode 22 and a workpiece 24 are placed facing each other. The machining fluid circulation device 20 includes a drain fluid tank 26 to which machining fluid 10 containing sludge is delivered after electrical discharge machining is performed in the machining tank 12, and a supply fluid tank 28 to supply the machining fluid 10 to the machining tank 12. have. The machining liquid 10 in the drain tank 26 is sent to a filter 14 made of paper, cloth, etc. by a pressure pump 30, and then divided and a portion is sent to the supply liquid tank 28. Divided supply liquid tank 2
The remainder sent to the activated carbon filtration tank 16 and the ion exchange tank 18 are passed through the electromagnetic valve 32 in the middle.
After being sent to the supply liquid tank 28, it is similarly sent to the supply liquid tank 28. The machining fluid 10 in the supply fluid tank 28 is sent to the machining tank 12 by a pressure pump 34, and a part of the machining fluid 10 is diverted and passed through a resistivity measuring device 36 to measure its resistivity value. In the figure, reference numeral 38 denotes a control box that opens and closes the electromagnetic valve 32 and adjusts the flow rate of the machining fluid 10 sent to the ion exchange tank 18 according to the resistivity value measured by the resistivity measuring device 36. Also, in the figure 40,
42 are valves that respectively adjust the flow rate of the machining fluid 10. Furthermore, between the activated carbon filtration tank 16 and the ion exchange tank 18, a filtration judgment device 44 for visual judgment is provided.
is provided.

次にこの従来装置の作用について説明すると、
放電加工を行なつた結果、スラツジを含むことと
なつた加工液10は、排液槽26に送り込まれ
る。この排液槽26中で、重いスラツジを沈澱さ
せ、軽いスラツジを含んだ加工液10が、圧力ポ
ンプ30にてフイルター14に送られて、2〜
1μのスラツジを含んだ加工液10として濾過さ
れる。この濾過された加工液10は、供給液槽2
8に送られ、更に圧力プンプ34にて、流量調整
用のバルブ40を通過して加工槽12へと循環さ
れる。又、この供給液槽28から加工槽12に送
られる加工液10の一部は分流され、比抵抗測定
器36にて比抵抗値を測定し、この値がコントロ
ールボツクス38に予め設定された値以下の場合
は電磁バルブ32を開き、フイルター14から供
給液槽28に送られる加工液10の一部を、活性
炭濾過槽16、イオン交換槽18と順次通過させ
て、2〜1μのスラツジを除去すると共に、比抵
抗値を上げ、供給液槽28中の加工液10全体の
比抵抗値を設定値に維持して加工槽12に送り込
むこととなる。又、活性炭濾過槽16からの加工
液10は、濾過判定器44を通過することとなる
ので、目視により活性炭の寿命判定が行なえる。
Next, we will explain the operation of this conventional device.
The machining fluid 10 containing sludge as a result of electrical discharge machining is sent to the drain tank 26 . In this drain tank 26, the heavy sludge is precipitated, and the machining liquid 10 containing light sludge is sent to the filter 14 by the pressure pump 30.
The processing liquid 10 containing 1 μm of sludge is filtered. This filtered machining fluid 10 is supplied to the supply fluid tank 2
8, and is further circulated to the processing tank 12 by the pressure pump 34, passing through a valve 40 for adjusting the flow rate. Further, a part of the machining fluid 10 sent from the supply fluid tank 28 to the machining tank 12 is diverted, and a resistivity value is measured by a resistivity measuring device 36, and this value is set as a value preset in the control box 38. In the following cases, open the electromagnetic valve 32 and let a part of the processing fluid 10 sent from the filter 14 to the supply fluid tank 28 pass through the activated carbon filtration tank 16 and the ion exchange tank 18 in order to remove 2 to 1 μm of sludge. At the same time, the specific resistance value is increased to maintain the specific resistance value of the entire machining fluid 10 in the supply fluid tank 28 at the set value, and the machining fluid 10 is fed into the machining tank 12. Furthermore, since the machining fluid 10 from the activated carbon filtration tank 16 passes through the filtration determination device 44, the lifespan of the activated carbon can be visually determined.

しかしながら、この種の加工液循環装置20に
あつては、使用の結果による加工液10の消耗、
即ち有機化合物を含んだ加工液10の濃度測定が
人の手によつて行なわれることとなつており、作
業性が悪いだけでなく、その測定結果によつて、
水あるいは有機化合物の補充量をその都度計算し
なければならない煩わしさがあつた。
However, in this type of machining fluid circulation device 20, consumption of the machining fluid 10 due to use,
In other words, the concentration of the processing liquid 10 containing organic compounds is to be measured manually, which not only has poor workability but also makes it difficult for the measurement results to
It was troublesome to have to calculate the amount of water or organic compound to be replenished each time.

本発明はこのような課題に鑑み為されたもので
あり、その目的は、加工液の濃度測定を容易に行
なえる様にして、常に最良の状態で加工が行なえ
る放電加工装置を提供することにある。
The present invention has been made in view of these problems, and its purpose is to provide an electric discharge machining device that allows machining fluid concentration to be easily measured and machining to be performed in the best possible condition at all times. It is in.

上記目的を達成する為に、本発明は、水と有機
化合物との溶液から成る加工液中で放電加工を行
なう加工槽と、加工液中のスラツジ除去を行なう
フイルター、活性炭濾過槽及び比抵抗値を向上さ
せるイオン交換槽をその途中に配した加工液循環
装置とこの加工液循環装置中に、活性炭濾過槽通
過後の加工液の有機化合物濃度測定装置とを備え
たことを特徴とする。
In order to achieve the above object, the present invention provides a machining tank for performing electric discharge machining in a machining fluid consisting of a solution of water and an organic compound, a filter for removing sludge from the machining fluid, an activated carbon filter tank, and a specific resistance value. The present invention is characterized by comprising a machining fluid circulation device having an ion exchange tank disposed midway therein, and a device for measuring the concentration of organic compounds in the machining fluid after passing through an activated carbon filtration tank, in the machining fluid circulation device.

以下、図面に基づいて本発明の好適な実施例を
説明する。
Hereinafter, preferred embodiments of the present invention will be described based on the drawings.

本発明は、第2図に示してあり、第1図と同一
部材には同一符号を付して説明を省略する。
The present invention is shown in FIG. 2, and the same members as in FIG. 1 are given the same reference numerals, and their explanation will be omitted.

活性炭濾過槽16を通過した加工液10は、濾
過判定器44を介してイオン交換槽18に送られ
るが、本発明では、活性炭濾過槽16と、イオン
交換槽18との間に、濾過判定器44とは別に、
加工液10の濃度測定装置46が設けてある。
The processing liquid 10 that has passed through the activated carbon filtration tank 16 is sent to the ion exchange tank 18 via the filtration determination device 44, but in the present invention, a filtration determination device is provided between the activated carbon filtration tank 16 and the ion exchange tank 18. Apart from 44,
A concentration measuring device 46 for the processing fluid 10 is provided.

次に本発明に係る装置の作用について説明する
と、放電加工を行なつた結果、スラツジを含むこ
ととなつた加工液10は、排液槽26に送り込ま
れる。この排液槽26中で、重いスラツジを沈澱
させ、軽いスラツジを含んだ加工液10が、圧力
ポンプ30にてフイルター14に送られて、2〜
1μのスラツジを含んだ加工液10として濾過さ
れる。この濾過された加工液10は、供給液槽2
8に送られ、更に圧力ポンプ34にて、流量調整
用のバルブ40を通過して加工槽12へと循環さ
れる。又、この供給液槽28から加工槽12に送
られる加工液10の一部は分流され、比抵抗測定
器36にて比抵抗値を測定し、この値がコントロ
ールボツクス38に予め設定された値以下の場合
は電磁バルブ32を開き、フイルター14から供
給液槽28に送られる加工液10の一部を、活性
炭濾過槽16、イオン交換槽18と順次通過させ
て、2〜1μのスラツジを除去すると共に、比抵
抗値を上げ、供給液槽28中の加工液10全体の
比抵抗値を設定値に維持して加工槽12に送り込
むこととなる。ここで、本発明においては、加工
液循環装置20中に活性炭濾過槽16を設けたの
で、従来除去できないとされていた2〜1μ以下
のスラツジ及び不純物の吸着除去が行える。この
ため、活性炭濾過槽16より得られる加工液10
中の色素成分等の微量有機物やスラツジ及び不純
物の除去が高度に行なわれるため、イオン交換槽
18においてイオン交換樹脂にスラツジ等が吸着
されることがなく、イオン交換樹脂の寿命延長及
び性能維持が図れる。
Next, the operation of the apparatus according to the present invention will be described. As a result of electrical discharge machining, the machining fluid 10 containing sludge is sent to the drain tank 26. In this drainage tank 26, the heavy sludge is precipitated, and the machining liquid 10 containing light sludge is sent to the filter 14 by the pressure pump 30.
The processing liquid 10 containing 1 μm of sludge is filtered. This filtered machining fluid 10 is supplied to the supply fluid tank 2
8, and is further circulated by the pressure pump 34 to the processing tank 12 through a flow rate adjustment valve 40. Further, a part of the machining fluid 10 sent from the supply fluid tank 28 to the machining tank 12 is diverted, and a resistivity value is measured by a resistivity measuring device 36, and this value is set as a value preset in the control box 38. In the following cases, open the electromagnetic valve 32 and let a part of the processing fluid 10 sent from the filter 14 to the supply fluid tank 28 pass through the activated carbon filtration tank 16 and the ion exchange tank 18 in order to remove 2 to 1 μm of sludge. At the same time, the specific resistance value is increased to maintain the specific resistance value of the entire machining fluid 10 in the supply fluid tank 28 at the set value, and the machining fluid 10 is fed into the machining tank 12. Here, in the present invention, since the activated carbon filtration tank 16 is provided in the machining fluid circulation device 20, it is possible to adsorb and remove sludge and impurities of 2 to 1 μm or less, which were conventionally considered impossible to remove. For this reason, the processing liquid 10 obtained from the activated carbon filtration tank 16
Since trace amounts of organic matter such as pigment components, sludge, and impurities are removed to a high degree, sludge and the like are not adsorbed to the ion exchange resin in the ion exchange tank 18, extending the life of the ion exchange resin and maintaining its performance. I can figure it out.

なお、具体的には、本発明の活性炭濾過槽16
を設けたことでイオン交換樹脂の寿命が1.3〜1.4
倍程度度のびるというデータが得られている。つ
まり、イオン交換樹脂51を用い、比抵抗測定器
34による加工液10の比抵抗10×104Ωmで活
性炭濾過槽16、イオン交換槽14への通過を制
御した場合、当初11×104Ωmであつた加工液10
の比抵抗が8×104Ωm以下となるまでの被加工
物の加工量(処理期間に対応する)は、活性炭濾
過槽42のない場合7Kgであつたのが、活性炭濾
過層42を設けたことによつて10Kg程度にのび
た。
In addition, specifically, the activated carbon filtration tank 16 of the present invention
The life of the ion exchange resin is 1.3 to 1.4
Data has been obtained that the effect is increased by about twice as much. In other words, when using the ion exchange resin 51 and controlling the passage of the machining fluid 10 to the activated carbon filtration tank 16 and the ion exchange tank 14 with a specific resistance of 10×10 4 Ωm measured by the specific resistance measuring device 34, the initial resistivity of the machining fluid 10 is 11×10 4 Ωm. Hot processing fluid 10
The processing amount (corresponding to the processing period) of the workpiece until the specific resistance of the workpiece becomes 8×10 4 Ωm or less was 7 kg without the activated carbon filtration tank 42, but with the activated carbon filtration layer 42 In some cases, it grew to about 10kg.

このように、活性炭濾過槽16を設けることに
よつて、イオン交換樹脂に付着するスラツジ等の
量を非常に少なくでき、イオン交換樹脂の本来の
能力を十分に発揮させることができるという効果
が得られる。
As described above, by providing the activated carbon filter tank 16, the amount of sludge etc. that adheres to the ion exchange resin can be greatly reduced, and the effect that the original ability of the ion exchange resin can be fully exhibited is obtained. It will be done.

そして、この発明では活性炭濾過槽16からの
加工液10は、濾過判定器44を通過するだけで
なく濃度測定装置46を通過する。このため、濾
過判定器44における目視による活性炭の寿命判
定が行えるだけでなく、加工液10中の有機化合
物濃度が判定できる。そこで、加工液10中の有
機物濃度が薄い場合は濃縮加工液の補給を、濃い
場合は水の補給を行うことができる。
In the present invention, the processing fluid 10 from the activated carbon filtration tank 16 not only passes through the filtration determiner 44 but also passes through the concentration measuring device 46 . Therefore, not only can the lifespan of the activated carbon be visually determined by the filtration determining device 44, but also the concentration of organic compounds in the processing fluid 10 can be determined. Therefore, when the concentration of organic matter in the processing liquid 10 is low, concentrated processing liquid can be replenished, and when it is high, water can be replenished.

このように、本発明によれば、加工液循環装置
20中にスラツジ等の除去後の加工液10の濃度
測定装置46を設けたので、濃縮加工液あるいは
水等の補給によつて、常に加工液10を最良の状
態に保つことができ、放電加工の精度の向上が望
めるものである。
As described above, according to the present invention, since the device 46 for measuring the concentration of the machining fluid 10 after removing sludge or the like is provided in the machining fluid circulation device 20, the machining fluid can be constantly replenished by replenishing concentrated machining fluid or water. The liquid 10 can be maintained in the best condition, and the accuracy of electrical discharge machining can be improved.

さらに、濃度測定装置46は活性炭濾過槽16
の後に設けてある。このため、この濃度測定装置
46に流入する加工液10は2〜1μ以下の非常
に微細なスラツジ等も除去されている。そこで、
加工液中の有機加工化合物の濃度を正確に測定す
ることができる。
Furthermore, the concentration measuring device 46 is connected to the activated carbon filtration tank 16.
It is located after. Therefore, very fine sludge of 2 to 1 μm or less is also removed from the processing fluid 10 flowing into the concentration measuring device 46. Therefore,
It is possible to accurately measure the concentration of organic processing compounds in the processing fluid.

つまり、加工液10に混合される有機化合物
は、通常糖類であるが、この濃度測定において、
浮遊性のスラツジ等は悪影響を及ぼす。また、糖
類の濃度測定に利用される光学的方法においては
色素成分の影響も大きい。ところが、この発明に
あつては、これら測定に悪影響を及ぼす不純物の
ほとんどが活性炭濾過槽16で除去されており、
非常に正確な有機化合物の濃度測定が行える。
In other words, the organic compound mixed in the processing liquid 10 is usually sugar, but in this concentration measurement,
Floating sludge etc. have an adverse effect. Furthermore, in the optical method used to measure the concentration of sugars, the influence of pigment components is also large. However, in the present invention, most of the impurities that adversely affect these measurements are removed in the activated carbon filtration tank 16.
Very accurate concentration measurements of organic compounds can be made.

次に、濃度測定装置46及び、該装置46の測
定結果を表示する表示装置48の一実施例を、第
2図、第3図に従つて説明する。
Next, an embodiment of the concentration measuring device 46 and the display device 48 that displays the measurement results of the device 46 will be described with reference to FIGS. 2 and 3.

濃度測定装置46は、スラツジ除去後の加工液
10を通過させる透光パイプ50と、このパイプ
50の一側に設けた光源52と、他側に設けた複
数の受光部54とから構成され、光源52への通
電は、タイマー56を用い、一定間隔で行なわれ
る様に形成してある。一方、表示装置48は、コ
ントロールボツクス38に併設されており、濃度
測定装置46に設けた複数の受光部54に対応す
るランプ58と、該ランプ58の表側に設けてあ
る透光表示板60とから形成されている。
The concentration measuring device 46 is composed of a transparent pipe 50 through which the machining liquid 10 after sludge removal passes, a light source 52 provided on one side of the pipe 50, and a plurality of light receiving sections 54 provided on the other side. A timer 56 is used to energize the light source 52 at regular intervals. On the other hand, the display device 48 is attached to the control box 38, and includes a lamp 58 corresponding to the plurality of light receiving sections 54 provided in the concentration measuring device 46, and a transparent display plate 60 provided on the front side of the lamp 58. is formed from.

これらの装置の作用は、タイマー56によつて
定期的に通電された光源52の光が、透光パイプ
50中の加工液10を通して受光部54に達する
が、この時光の屈折によつて複数ある受光部54
の内のどの受光部54に光が達したかを、ランプ
58及び透光表示板60によつて表示して、加工
液10の有機化合物の濃度を測定するものであ
る。
The operation of these devices is such that the light from the light source 52 that is periodically energized by the timer 56 passes through the processing liquid 10 in the transparent pipe 50 and reaches the light receiving section 54, but at this time, due to the refraction of the light, there are multiple Light receiving section 54
The concentration of the organic compound in the processing liquid 10 is measured by displaying which of the light receiving parts 54 the light has reached using the lamp 58 and the transparent display plate 60.

なお、透光表示板60は加工液中の有機化合物
濃度を測定結果として表示するものであるが、こ
の測定結果の表示として、有機化合物の濃度が適
当ではなく補充物の補充が必要であるかのどうか
の表示としてもよく、さらにこの補充物が水であ
るか有機化合物が濃縮して含まれている濃縮加工
液であるかの区別と補充量とを同時に表示しても
よい。
The translucent display plate 60 displays the concentration of organic compounds in the processing fluid as a measurement result, but the measurement results may indicate whether the concentration of organic compounds is inappropriate and whether replenishment is required. Furthermore, whether the replenisher is water or a concentrated processing fluid containing concentrated organic compounds and the amount of replenishment may be displayed at the same time.

この様に、濃度測定装置46に表示装置48を
連動させると、使用し易く、かつ不良の加工液1
0使用等の事故がない。又表示装置48に、補充
物の区別と補充量とを表示する様に形成すると、
作業性が著しく向上する。更に、タイマー56を
用いて、濃度測定を定期的に行なう様にすると、
省電力に寄与するだけでなく、作業効率も高い。
In this way, by interlocking the display device 48 with the concentration measuring device 46, it is easy to use and it is easy to detect defective machining fluids.
There have been no accidents due to use of 0. Furthermore, if the display device 48 is formed to display the type of replenishment and the amount of replenishment,
Work efficiency is significantly improved. Furthermore, if the timer 56 is used to periodically measure the concentration,
Not only does it contribute to power savings, but it also has high work efficiency.

なお、濃度測定装置46は、前述の様に光を用
いなくても、歪、比重、トルク等を測定する様に
形成することもできる。
Note that the concentration measuring device 46 can also be formed to measure strain, specific gravity, torque, etc. without using light as described above.

又、本発明は、ワイヤカツト放電加工機の加工
液循環装置に応用できることは無論である。
Furthermore, it goes without saying that the present invention can be applied to a machining fluid circulation device for a wire-cut electrical discharge machine.

以上述べたように、本発明によれば、加工液循
環装置中に活性炭濾過槽及び有機化合物の濃度測
定装置とその表示装置を設けたため、加工液中の
有機化合物濃度を正確に把握でき、加工液を常に
最良の状態に保つことができ、放電加工の精度の
向上が図れる。
As described above, according to the present invention, since the activated carbon filtration tank, the organic compound concentration measuring device, and its display device are provided in the machining fluid circulation device, the organic compound concentration in the machining fluid can be accurately grasped, and the The liquid can always be kept in the best condition, improving the accuracy of electrical discharge machining.

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

第1図は従来装置の系統図、第2図は本発明装
置の系統図、第3図は濃度測定装置と表示装置と
の関連を示す概略図である。 各図中同一部材には同一符号を付し、10は加
工液、12は加工槽、14はフイルター、16は
活性炭濾過槽、18はイオン交換槽、20は加工
液循環装置、46は濃度測定装置、48は表示装
置である。
FIG. 1 is a system diagram of the conventional device, FIG. 2 is a system diagram of the device of the present invention, and FIG. 3 is a schematic diagram showing the relationship between the concentration measuring device and the display device. In each figure, the same members are given the same symbols, 10 is the machining fluid, 12 is the machining tank, 14 is the filter, 16 is the activated carbon filtration tank, 18 is the ion exchange tank, 20 is the machining fluid circulation device, and 46 is the concentration measurement. The device 48 is a display device.

Claims (1)

【特許請求の範囲】 1 水と有機化合物との溶液から成る加工液中で
放電加工を行う加工槽と、加工液中のスラツジ除
去を行なうフイルター、活性炭濾過槽及び比抵抗
値を向上させるイオン交換槽をその途中に配した
加工液循環装置と、この加工液循環装置中に、上
記活性炭濾過槽通過後の加工液の有機化合物の濃
度を測定する濃度測定装置と、この濃度測定装置
における測定結果を表示する表示装置とを備えた
ことを特徴とする放電加工装置。 2 特許請求の範囲1項の装置において、表示装
置を、加工液への補充の要否を表示するように形
成したことを特徴とする放電加工装置。 3 特許請求の範囲2の装置において、表示装置
を、補充物の区別と補充量とを表示するように形
成したことを特徴とする放電加工装置。
[Claims] 1. A machining bath for performing electric discharge machining in a machining fluid consisting of a solution of water and an organic compound, a filter for removing sludge from the machining fluid, an activated carbon filtration tank, and an ion exchanger for improving specific resistance. A machining fluid circulation device with a tank disposed in the middle thereof, a concentration measuring device in the machining fluid circulation device for measuring the concentration of organic compounds in the machining fluid after passing through the activated carbon filtration tank, and a measurement result of the concentration measuring device. An electrical discharge machining device comprising: a display device that displays the following. 2. An electric discharge machining apparatus according to claim 1, characterized in that the display device is formed to display whether or not the machining fluid needs to be replenished. 3. The electric discharge machining apparatus according to claim 2, wherein the display device is formed to display the distinction between replenishers and the amount of replenishment.
JP7067480A 1980-05-27 1980-05-27 Discharge processing device Granted JPS571619A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7067480A JPS571619A (en) 1980-05-27 1980-05-27 Discharge processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7067480A JPS571619A (en) 1980-05-27 1980-05-27 Discharge processing device

Publications (2)

Publication Number Publication Date
JPS571619A JPS571619A (en) 1982-01-06
JPH0134730B2 true JPH0134730B2 (en) 1989-07-20

Family

ID=13438426

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7067480A Granted JPS571619A (en) 1980-05-27 1980-05-27 Discharge processing device

Country Status (1)

Country Link
JP (1) JPS571619A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62259717A (en) * 1986-05-01 1987-11-12 Ibuki Denshi Seiki:Kk Machining waste water purification method for wire-cut electric discharge machining and device thereof
JP2010099648A (en) * 2008-09-26 2010-05-06 Ryoden Koki Engineering Kk Water purifier

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5226357A (en) * 1975-08-26 1977-02-26 Itakura Kougiyou Yuugen Method of forming thrust washers

Also Published As

Publication number Publication date
JPS571619A (en) 1982-01-06

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