JPH0134731B2 - - Google Patents
Info
- Publication number
- JPH0134731B2 JPH0134731B2 JP55072003A JP7200380A JPH0134731B2 JP H0134731 B2 JPH0134731 B2 JP H0134731B2 JP 55072003 A JP55072003 A JP 55072003A JP 7200380 A JP7200380 A JP 7200380A JP H0134731 B2 JPH0134731 B2 JP H0134731B2
- Authority
- JP
- Japan
- Prior art keywords
- machining
- tank
- fluid
- machining fluid
- concentration
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23H—WORKING 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
- B23H1/00—Electrical 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
- B23H1/10—Supply or regeneration of working media
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- Filtration Of Liquid (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
を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 electric discharge machining apparatus, and more particularly to an electric discharge machining apparatus that performs electric discharge machining on a workpiece in a machining fluid containing organic compounds mixed with water at a proportion that does not burn them.
一般に、加工液を用いる放電加工装置は、加工
に伴つて循環させている加工液の濃度が変化し、
それが為、加工性能あるいは加工精度の低下を来
たしていた。そこでこの種の装置において、加工
液の循環装置中に、加工液の濃度測定装置を付設
し、この濃度測定装置の測定結果を、適宜表示装
置に、補充の要、不要及び、補充液の種類、量の
表示として示す様に形成することについて先に提
案した。 Generally, in electric discharge machining equipment that uses machining fluid, the concentration of the machining fluid being circulated changes as machining is performed.
This has caused a decline in machining performance or machining accuracy. Therefore, in this type of equipment, a processing fluid concentration measuring device is attached to the processing fluid circulation device, and the measurement results of this concentration measuring device are displayed on an appropriate display device, indicating whether replenishment is required or not, and the type of replenishing fluid. , it was previously proposed to form it as shown as an indication of quantity.
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
装置があつた。。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2
6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28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及び、加工液10の濃度測定装置46が
設けてある。なお、コントロールボツクス38に
付設した表示装置48は、濃度測定装置46の測
定結果によつて、補充の要、不要及び、補充液の
種類、量として表示するものである。 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. There was a device consisting of an activated carbon filtration tank 16 and a machining fluid circulation device 20 that circulates the machining fluid 10 by disposing an ion exchange tank 18 for improving the specific resistance value of the machining fluid 10 in the middle thereof. . In the machining liquid 10 in the machining tank 12,
The electrode 22 and the workpiece 24 are positioned facing each other. The machining fluid circulation device 20 includes a drain fluid tank 26 to which machining fluid 10 containing sludge is fed 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. Drainage tank 2
The processing liquid 10 in 6 is sent by a pressure pump 30 to a filter 14 made of paper, cloth, etc., and then divided and a part of it is sent to a supply liquid tank 28. The remainder that is diverted and sent to the supply liquid tank 28 is sent to the electromagnetic valve 32
The liquid is sent to the activated carbon filtration tank 16 and the ion exchange tank 18 in sequence via the
sent to. 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 the 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. Further, numerals 40 and 42 in the figure are valves that respectively adjust the flow rate of the machining fluid 10. Further, between the activated carbon filtration tank 16 and the ion exchange tank 18, a filtration determination device 44 for visual determination and a concentration measuring device 46 for the processing liquid 10 are provided. A display device 48 attached to the control box 38 displays whether replenishment is required or not, as well as the type and amount of replenisher, based on the measurement results of the concentration measuring device 46.
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12に送り込まれ
る。この排液槽12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。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、目視による活性炭の寿命判定が行なえるだ
けでなく、濃度測定装置46をも通過し、その測
定結果を表示装置48に表示するので、水あるい
は有機化合物等の補充が容易に行なえる。なお、
濃度測定装置46は、適宜時間間隔をおいて作動
させると、省電力等に寄与するものである。 Next, we will explain the operation of this conventional device.
Machining fluid 10 containing sludge as a result of electrical discharge machining is sent to drain tank 12 . In this drain tank 12, 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 fluid 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. Furthermore, since the machining liquid 10 from the activated carbon filtration tank 16 passes through the filtration determination device 44, it is not only possible to visually determine the lifespan of the activated carbon, but also passes through the concentration measurement device 46, and the measurement results are is displayed on the display device 48, so that water, organic compounds, etc. can be easily replenished. In addition,
When the concentration measuring device 46 is operated at appropriate time intervals, it contributes to power saving and the like.
しかしながら、このような加工液循環装置20
にあつては、加工液10の濃度測定及び表示が自
動化されるものの、補充はその都度表示された種
類の補充物を表示量だけ人力によつて行なわなけ
ればならず、補充の為の人間を必要とし、生産性
が著しく低いものであつた。 However, such a machining fluid circulation device 20
In this case, although the concentration measurement and display of the processing fluid 10 are automated, replenishment must be done manually each time using the indicated amount of replenisher of the indicated type, which requires a human being for replenishment. However, the productivity was extremely low.
本発明は前述した先の提案についての課題に鑑
み為されたものであり、その目的は、加工液の濃
度測定に連動して補充液を自動的に補充し、生産
性を向上させると共に、常に最良の状態の加工液
を用いて放電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 was created in view of the problems with the previous proposal, and its purpose is to automatically replenish the replenisher fluid in conjunction with the measurement of the concentration of the machining fluid, improve productivity, and constantly improve productivity. It is an object of the present invention to provide an electrical discharge machining device that can perform electrical discharge machining using machining fluid in the best condition.
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すると共に、前
記活性炭濾過通過後の加工液の有機化合物濃度を
測定する濃度測定装置を設けた加工液循環装置
と、前記濃度測定装置からの信号によつて加工液
の濃度を一定に制御する加工液の補充装置とを備
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. A machining fluid circulation device is provided with an ion exchange tank disposed midway therein, and a concentration measuring device for measuring the organic compound concentration of the machining fluid after passing through the activated carbon filtration; and a machining fluid replenishment device that controls the concentration of the machining fluid to be constant.
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 explanations will be omitted.
本発明では、従来装置に、加工液10の補充装
置50が設けてある。この補充装置50は、濃縮
した加工液10を溜めておく濃縮液槽52と、こ
の濃縮液槽52中の加工液10を供給液槽28に
送る圧力ポンプ54と、水の供給管56及びバル
ブ58とを、濃度測定装置46からの測定結果を
示す信号によつて作動する様に形成してある。 In the present invention, a replenishing device 50 for the machining fluid 10 is provided in the conventional device. This replenishing device 50 includes a concentrated liquid tank 52 that stores the concentrated processing liquid 10, a pressure pump 54 that sends the processed liquid 10 in the concentrated liquid tank 52 to the supply liquid tank 28, a water supply pipe 56, and a valve. 58 is configured to be activated by a signal indicating the measurement result from the concentration measuring device 46.
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 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 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.
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
よる活性炭の目視判定が行なえるだけでなく、濃
度測定装置46をも通過するので、加工液10中
の有機化合物濃度の判定が行なえる。この判定結
果として、例えば濃度が薄い場合は、濃縮液槽5
2の圧力ポンプ54を作動させて、濃縮加工液1
0を供給液槽28に送る様に補充装置50を作動
させ、濃度が濃い場合は、バルブ58を開放して
供給液槽28に水を送る様に補充装置50を作動
させるものである。 Furthermore, since the machining fluid 10 from the activated carbon filtration tank 16 passes through the filtration determination device 44, not only can the activated carbon be visually determined, but it also passes through the concentration measuring device 46, so the machining fluid 10 passes through the filtration determination device 44. The concentration of organic compounds in 10 can be determined. As a result of this determination, for example, if the concentration is low, the concentrated liquid tank 5
2 pressure pump 54 is operated to supply the concentrated processing liquid 1.
The replenishing device 50 is operated to send water to the supply liquid tank 28, and when the concentration is high, the valve 58 is opened and the replenishment device 50 is operated to send water to the supply liquid tank 28.
本発明は、加工液循環装置20中に、加工液1
0の濃度測定装置46を設けると共に、この濃度
測定装置46の測定結果によつて加工液10中
に、水または濃縮加工液10を自動的に供給する
補充装置50を設けたので、補充が自動的に行な
われ、生産性の向上が図れると共に、加工液10
の濃度を、理想的な一定値に保つことができ、放
電加工の性能及び精度を向上させることができ
る。 In the present invention, the machining fluid 1 is provided in the machining fluid circulation device 20.
0 concentration measuring device 46 and a replenishing device 50 that automatically supplies water or concentrated machining fluid 10 into the machining fluid 10 based on the measurement result of the concentration measuring device 46, replenishment is automatic. In addition to improving productivity, the machining fluid can be
concentration can be maintained at an ideal constant value, and the performance and accuracy of electric discharge machining can be improved.
なお、濃度測定装置46は活性炭濾過槽16の
後段に設けてある。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。 Note that the concentration measuring device 46 is provided downstream of the activated carbon filtration tank 16. 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.
又、濃縮液槽52中に液量計(周知の為図示せ
ず)を設け、濃縮液槽52中の加工液10が一定
以下となつた時にこれを示すランプ60をコント
ロールボツクス38に設けると共に、コントロー
ルボツクス38に設けたスイツチ62の操作によ
り、圧力ポンプ54で濃縮液槽52内の加工液1
0を汲み上げて、再び濃縮液槽52内に噴射する
様に形成した、水と有機化合物との溶解装置64
を付設すると、水と有機化合物との溶解が完全に
行なえるだけでなく、溶解が自動的に行なえるの
で便利である。なお、第2図中66は、溶解作業
を一定時間のみ行なわせる為のタイマーであり、
68は、濃縮液槽52中の加工液10を、供給液
槽28に送る場合に開くバルブであり、70は、
溶解作業を行なう場合に開くバルブである。 Further, a liquid level meter (not shown because it is well known) is provided in the concentrated liquid tank 52, and a lamp 60 is provided in the control box 38 to indicate when the processing liquid 10 in the concentrated liquid tank 52 is below a certain level. By operating the switch 62 provided in the control box 38, the pressure pump 54 pumps the machining liquid 1 in the concentrated liquid tank 52.
A dissolving device 64 for dissolving water and organic compounds, which is configured to draw up 0 and inject it into the concentrated liquid tank 52 again.
When attached, it is convenient because not only can the water and organic compound be completely dissolved, but also the dissolution can be done automatically. In addition, 66 in Fig. 2 is a timer to allow the melting work to be performed only for a certain period of time.
68 is a valve that opens when the processing liquid 10 in the concentrated liquid tank 52 is sent to the supply liquid tank 28;
This is a valve that opens when performing melting work.
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濃度測定装置を設け
るとともにこの濃度測定装置の測定結果によつて
補充装置を自動的に動作させるため、加工液中の
有機化合物濃度を自動的に常に一定に保つことが
でき、特に水の蒸発等によつて有機化合物の濃度
が変化した場合においてもこれを自動的に補正で
き加工液中の有機化合物濃度を一定に保つことが
できる。これによつて常に最適の状態で放電加工
が行える。 As described above, according to the present invention, an activated carbon filtration tank and a concentration measuring device are provided in the machining fluid circulation device, and the replenishing device is automatically operated based on the measurement results of the concentration measuring device. The concentration of organic compounds in the processing fluid can be automatically kept constant at all times, and even if the concentration of organic compounds changes due to water evaporation, etc., this can be automatically corrected. can be kept constant. This allows electrical discharge machining to be performed in the optimum condition at all times.
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、50は補充装
置、52は濃縮液槽、64は溶解装置である。
FIG. 1 is a system diagram of a conventional device, and FIG. 2 is a system diagram of the device of the present invention. 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. 50 is a replenishing device, 52 is a concentrated liquid tank, and 64 is a dissolving device.
Claims (1)
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す
ると共に、前記活性炭濾過槽通過後の加工液の有
機化合物濃度を測定する濃度測定装置を設けた加
工液循環装置と、前記濃度測定装置からの信号に
よつて加工液の有機化合物濃度を一定に制御する
加工液の補充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の装置において、補充装置
は、適量の水または濃縮液槽中の有機化合物の濃
縮液を加工液に補充できる様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、濃縮液槽
は、水と有機化合物との溶解装置及び、液量計を
備えたことを特徴とする放電加工装置。[Scope of 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 exchange for improving specific resistance. A machining fluid circulation device is provided with a tank in the middle, and a concentration measuring device for measuring the organic compound concentration of the machining fluid after passing through the activated carbon filtration tank; An electric discharge machining apparatus characterized by comprising a machining fluid replenishment device that controls the concentration of an organic compound to be constant. 2. The electric discharge machining apparatus according to claim 1, wherein the replenishing device is configured to replenish the machining fluid with an appropriate amount of water or a concentrated liquid of an organic compound in a concentrated liquid tank. 3. The electric discharge machining apparatus according to claim 2, wherein the concentrated liquid tank is equipped with a water and organic compound dissolving device and a liquid level meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7200380A JPS571623A (en) | 1980-05-29 | 1980-05-29 | Discharge processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7200380A JPS571623A (en) | 1980-05-29 | 1980-05-29 | Discharge processing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS571623A JPS571623A (en) | 1982-01-06 |
| JPH0134731B2 true JPH0134731B2 (en) | 1989-07-20 |
Family
ID=13476800
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7200380A Granted JPS571623A (en) | 1980-05-29 | 1980-05-29 | Discharge processing device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS571623A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0241820A (en) * | 1988-08-01 | 1990-02-13 | Fanuc Ltd | Water quality control device for wire-cut electric discharge machine |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5226357A (en) * | 1975-08-26 | 1977-02-26 | Itakura Kougiyou Yuugen | Method of forming thrust washers |
-
1980
- 1980-05-29 JP JP7200380A patent/JPS571623A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS571623A (en) | 1982-01-06 |
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