JPH061299Y2 - Electrolytic deburring device - Google Patents

Electrolytic deburring device

Info

Publication number
JPH061299Y2
JPH061299Y2 JP17189587U JP17189587U JPH061299Y2 JP H061299 Y2 JPH061299 Y2 JP H061299Y2 JP 17189587 U JP17189587 U JP 17189587U JP 17189587 U JP17189587 U JP 17189587U JP H061299 Y2 JPH061299 Y2 JP H061299Y2
Authority
JP
Japan
Prior art keywords
rust preventive
electrolytic
tank
electrolyte
preventive oil
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 - Lifetime
Application number
JP17189587U
Other languages
Japanese (ja)
Other versions
JPH0179528U (en
Inventor
正則 北村
定則 平野
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.)
Chuo Seisakusho KK
Original Assignee
Chuo Seisakusho KK
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 Chuo Seisakusho KK filed Critical Chuo Seisakusho KK
Priority to JP17189587U priority Critical patent/JPH061299Y2/en
Publication of JPH0179528U publication Critical patent/JPH0179528U/ja
Application granted granted Critical
Publication of JPH061299Y2 publication Critical patent/JPH061299Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Description

【考案の詳細な説明】 (産業上の利用分野) 本考案は電解バリ取り装置の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to an improved electrolytic deburring device.

(従来の技術) 従来の電解バリ取り装置は電解バリ取り工程と防錆処理
工程の間に水洗工程を組込んだもので、第2図に示すよ
うに各工程を夫々独立させ、電解バリ取りステーション
(51)、水洗ステーション(52)、防錆ステーション(53)に
ワーク(54)を順次搬送する構造のものであった。
(Prior Art) A conventional electrolytic deburring device incorporates a water washing step between the electrolytic deburring step and the rustproofing step. As shown in FIG. station
The structure was such that the work (54) was sequentially transported to the (51), the water washing station (52), and the rust prevention station (53).

(考案が解決しようとする問題点) しかしこのような従来のものにあっては、ワーク(54)を
各ステーションへ搬送しなければならず、また、有用な
電解液が失われる上、水洗水の廃水処理を必要とする問
題もある。そこでワーク(54)の搬送を少なくし、電解液
の回収を効率的に行える電解バリ取り装置の開発が待望
されている。
(Problems to be solved by the invention) However, in such a conventional one, the work (54) has to be transported to each station, useful electrolyte is lost, and washing water is used. There is also a problem that requires wastewater treatment. Therefore, it is desired to develop an electrolytic deburring device that can efficiently transport the electrolyte solution by reducing the transportation of the work (54).

(問題点を解決するための手段) 本考案は前記のような待望に応えてなされたもので電解
液槽と電極との間を電解液供給管により接続するととも
に、該電極と遠心分離機との間を電解液排出管により接
続し、さらに遠心分離機と前記電解液槽とを電解液返却
管により接続させた電解バリ取りステーションと、電解
バリ取りされたワークをセットする治具と防錆油槽との
間を防錆油を供給する防錆油供給管により接続するとと
もに前記治具と防錆油槽との間を防錆油を返送する防錆
油排出管により接続した防錆ステーションを備え、さら
に前記電解液槽と電解液返却管を介して接続されている
遠心分離機と防錆油槽の底部とを返却管により接続した
ことを特徴とするものである。
(Means for Solving the Problems) The present invention has been made in response to the above-mentioned long-awaited situation, and the electrolytic solution supply pipe is connected between the electrolytic solution tank and the electrode, and the electrode and the centrifuge are connected to each other. Between them by an electrolytic solution discharge pipe, and further, an electrolytic deburring station in which a centrifugal separator and the electrolytic solution tank are connected by an electrolytic solution return pipe, a jig for setting the electrolytic deburred work, and rust prevention. It is equipped with an anticorrosion station that connects the oil tank with an antirust oil supply pipe that supplies antirust oil and also connects the jig and the antirust oil tank with an antirust oil discharge pipe that returns antirust oil. The centrifuge, which is connected to the electrolytic solution tank via the electrolytic solution return pipe, and the bottom of the rust preventive oil tank are connected by a return pipe.

(実施例) 次に、本考案の実施例を第1図により詳細に説明する。
先ず、ワークの電解バリ取りを行う電解バリ取りステー
ション(1)について説明すれば、(2)はワーク(3)のバリ
取り面に相応した電極、(4)はワーク(3)に給電するため
の給電加圧部、(5)は電極(2)とワーク(3)に直流電流を
印加する直流電源、(6)は電極(2)に先端を接続させると
ともに基端を電解液槽(7)に接続させた電解液供給管で
あり、該電解液供給管(6)には電解液の送給および停止
を行う電磁弁(8)と流量計(9)およびフィルター(10)が設
けられているとともに、ポンプ(11)が設けられている。
(12)は電解液供給管(6)のポンプ(11)の上方位置から分
岐した余剰電解液返却管であり、該余剰電解液返却管(1
2)は余剰の電解液を電解液槽(7)に循環させて該電解液
槽(7)内の電解液を撹拌させるものである。(13)は電極
(2)に基端を接続させた電解液排出管(14)を介して排出
された電解液中のスラッジを除去する遠心分離機、(15)
は遠心分離機(13)によりスラッジを除去した電解液を電
解液槽(7)に返却させる電解液返却管である。なお(16)
は電解バリ取り終了後にワーク(2)から電解液を除去す
るためにエアーを吹付けるエアー送給装置であり、該エ
アー送給装置(16)は電解液供給管(6)を介してエアーを
吹込むものとされている。また(17)は電解液槽(7)の電
解液の液面を監視するための電極式の液面計、(9a)、(9
b)は流量計(9)の監視下に電解液の供給量を制御する制
御弁である。
(Embodiment) Next, an embodiment of the present invention will be described in detail with reference to FIG.
First, the electrolytic deburring station (1) for electrolytic deburring of a work will be described. (2) is an electrode corresponding to the deburring surface of the work (3), and (4) is for supplying power to the work (3). (5) is a direct current power source for applying a direct current to the electrode (2) and the work (3), and (6) is the electrode (2) with its tip connected to the electrolyte tank (7). ) Is connected to the electrolytic solution supply pipe, the electrolytic solution supply pipe (6) is provided with a solenoid valve (8) for feeding and stopping the electrolytic solution, a flow meter (9) and a filter (10). In addition, a pump (11) is provided.
(12) is an excess electrolyte return pipe branched from the position above the pump (11) of the electrolyte supply pipe (6), and the excess electrolyte return pipe (1
In 2), the excess electrolytic solution is circulated in the electrolytic solution tank (7) to stir the electrolytic solution in the electrolytic solution tank (7). (13) is an electrode
Centrifuge for removing sludge in the electrolyte discharged through the electrolyte discharge pipe (14) with the proximal end connected to (2), (15)
Is an electrolytic solution return pipe for returning the electrolytic solution from which sludge has been removed by the centrifuge (13) to the electrolytic solution tank (7). (16)
Is an air feeding device that blows air to remove the electrolytic solution from the work (2) after completion of electrolytic deburring, and the air feeding device (16) blows air through the electrolytic solution supply pipe (6). It is supposed to be blown in. Further, (17) is an electrode-type liquid level gauge for monitoring the liquid level of the electrolytic solution in the electrolytic solution tank (7), (9a), (9
b) is a control valve that controls the amount of electrolyte supply under the supervision of the flow meter (9).

次に、ワークの防錆処理を行う防錆処理ステーション(1
8)について説明すれば、(19)は電解バリ取りステーショ
ン(1)から移送されてきた電解バリ取り直後のワーク(3)
をセットして該ワーク(3)に向け防錆油を流動させるた
めの治具、(20)はワーク押え、(21)は治具(19)に先端を
接続させるとともに基端を防錆油槽(22)に接続させた防
錆油供給管であり、該防錆油供給管(21)には防錆油を強
制的に送るポンプ(23)が設けられている。(24)は治具(1
9)とワーク(3)との間から排出された防錆油を防錆油槽
(22)に返送する防錆油排出管、(25)は防錆油によりワー
ク表面から洗い流され、防錆油槽(22)に流入して該防錆
油槽(22)の底に沈降した電解液を取り出して前記した遠
心分離機(13)に送給するポンプ(26)付の返却管、(27)は
液面計でオーバーフロー防止および電解液増加を検知す
るもので、電解液が一定以上となった場合にポンプ(26)
を作動させるもである。
Next, the rust prevention processing station (1
Explaining 8), (19) is the work (3) immediately after electrolytic deburring transferred from the electrolytic deburring station (1).
A jig for flowing rust preventive oil toward the work (3), (20) a work holder, and (21) a jig (19) with its tip connected to the base and a rust preventive oil tank. A rust preventive oil supply pipe connected to (22), and the rust preventive oil supply pipe (21) is provided with a pump (23) forcibly sending the rust preventive oil. (24) is the jig (1
The rust-preventive oil discharged from between the work piece (3) and the work piece (3)
Anti-corrosion oil discharge pipe returned to (22), (25) electrolytic solution washed from the work surface by anti-corrosion oil, flowed into the anti-corrosion oil tank (22) and settled at the bottom of the anti-corrosion oil tank (22) A return pipe with a pump (26) for taking out and feeding it to the above-mentioned centrifuge (13), (27) is a liquid level gauge for detecting overflow prevention and electrolyte increase, and the electrolyte is above a certain level. Pump in case of (26)
It also activates.

(作用) このように構成されたものは、先ず電解バリ取りステー
ション(1)においてワーク(3)を電極(2)に対応するよう
にセットするとともに給電加圧部(4)を該ワーク(3)に接
続する。次に、電磁弁(8)をONとして電解液槽(7)の電
解液をポンプ(11)により電解液供給管(6)の先端から電
極(2)とワーク(3)との間隙を流動させつつ直流電源(5)
により電極(2)に直流電流を印加してワーク(3)の電解バ
リ取りを行う。この電解バリ取り時に電極(2)とワーク
(3)との間から排出された電解液は電解液排出管(14)か
ら遠心分離機(13)に導いて、該遠心分離機(13)において
スラッジを除去したうえで再び電解液返却管(15)を介し
て電解液槽(7)に戻される。
(Operation) In the structure thus configured, first, the work (3) is set in the electrolytic deburring station (1) so as to correspond to the electrode (2), and the power supply pressurizing unit (4) is set to the work (3). ). Next, the solenoid valve (8) is turned on, and the electrolyte solution in the electrolyte solution tank (7) flows from the tip of the electrolyte solution supply pipe (6) through the gap between the electrode (2) and the work (3) by the pump (11). DC power supply (5)
By applying a DC current to the electrode (2), the electrolytic deburring of the work (3) is performed. During this electrolytic deburring, the electrode (2) and the workpiece
The electrolyte discharged from between (3) and (3) is introduced into the centrifuge (13) from the electrolyte discharge pipe (14), sludge is removed in the centrifuge (13), and then the electrolyte return pipe is returned. It is returned to the electrolytic solution tank (7) via (15).

この電解バリ取りが終了したらワーク(3)を水洗するこ
となく直ちに防錆処理ステーション(18)に搬送し、治具
(19)にワーク(3)をセットして該治具(19)に先端を接続
させた防錆油供給管(21)に設けたポンプ(23)を作動させ
て防錆油槽(22)内の防錆油を治具(19)からワーク(3)に
流動させる。これによりワーク(3)に防錆塗膜が形成さ
れるとともに該ワーク(3)に残留している電解液を洗い
流し、治具(19)と防錆油槽(22)との間に配設した排出管
(24)を介して防錆油槽(22)に返送すれば、電解液は防錆
油とは不溶で比重が重いため防錆油槽(22)の底部に沈降
することとなる。そこで該防錆油槽(22)の底部から返却
管(25)により電解液を抜き出して遠心分離機(13)に送
り、スラッジを除去したうえで電解液返却管(15)を通っ
て電解液槽(7)に返却する。このようにして電解液の回
収は確実に行われることとなる。
When this electrolytic deburring is completed, the work (3) is immediately transferred to the anticorrosion treatment station (18) without washing with water and the jig is
Inside the anticorrosion oil tank (22) by setting the work (3) in (19) and operating the pump (23) provided in the antirust oil supply pipe (21) whose tip is connected to the jig (19). The rust-preventing oil of is flowed from the jig (19) to the work (3). As a result, a rust preventive coating film is formed on the work (3) and the electrolytic solution remaining on the work (3) is washed away, and the work (3) is arranged between the jig (19) and the rust preventive oil tank (22). Discharge pipe
When it is returned to the rust preventive oil tank (22) through the (24), the electrolytic solution is insoluble in the rust preventive oil and has a large specific gravity, so that it will settle at the bottom of the rust preventive oil tank (22). Therefore, the electrolytic solution is extracted from the bottom of the rust preventive oil tank (22) by the return pipe (25) and sent to the centrifuge (13), sludge is removed, and then the electrolytic solution return pipe (15) is passed through. Return to (7). In this way, the recovery of the electrolytic solution is surely performed.

(考案の効果) 本考案は以上の説明によって明らかなように、ワークに
残留した微量の電解液を防錆処理ステーションにおいて
防錆油により洗い流し、防錆液槽に送って防錆油との性
状を巧妙に利用して防錆油槽の底部に沈降させたうえ遠
心分離機を介して電解液槽に返却するので電解液の回収
が効率的に行え、しかも水洗工程を略したので廃水処理
も不要となるもので、従来の電解バリ取り装置の問題点
を一掃したものとして、産業の発展に寄与するところは
極めて大である。
(Effect of the invention) As is apparent from the above explanation, the present invention rinses a small amount of the electrolytic solution remaining on the work with rust preventive oil at the rust preventive treatment station and sends it to the rust preventive solution tank to send it to the rust preventive oil. Is cleverly used to settle to the bottom of the rust preventive oil tank and then returned to the electrolytic solution tank via a centrifuge, so the electrolytic solution can be collected efficiently, and since the washing process is omitted, wastewater treatment is also unnecessary. Therefore, the problem of the conventional electrolytic deburring device is eliminated, and the contribution to the industrial development is extremely large.

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

第1図は本考案の実施例を示す概略的な断面図、第2図
は従来の電解バリ取り装置を示す概略的な断面図であ
る。 (1):電解バリ取りステーション、(2):電極、(3):ワ
ーク、(6):電解液供給管、(7):電解液槽、(13):遠心
分離機(14):電解液排出管、(15):電解液返却管、(1
8):防錆ステーション、(19):治具、(21):防錆油供給
管、(22):防錆油槽、(24):防錆油排出管、(25):返却
管。
FIG. 1 is a schematic sectional view showing an embodiment of the present invention, and FIG. 2 is a schematic sectional view showing a conventional electrolytic deburring apparatus. (1): Electrolytic deburring station, (2): Electrode, (3): Work, (6): Electrolyte supply pipe, (7): Electrolyte tank, (13): Centrifuge (14): Electrolysis Liquid discharge pipe, (15): Electrolyte return pipe, (1
8): Antirust station, (19): Jig, (21): Antirust oil supply pipe, (22): Antirust oil tank, (24): Antirust oil discharge pipe, (25): Return pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】電解液槽(7)と電極(2)との間を電解液供給
管(6)により接続するとともに、該電極(2)と遠心分離機
(13)との間を電解液排出管(14)により接続し、さらに遠
心分離機(13)と前記電解液槽(7)とを電解液返却管(15)
により接続させた電解バリ取りステーション(1)と、電
解バリ取りされたワーク(3)をセットする治具(19)と防
錆油槽(22)との間を防錆油を供給する防錆油供給管(21)
により接続するとともに前記治具(19)と防錆油槽(22)と
の間を防錆油を返送する防錆油排出管(24)により接続し
た防錆ステーション(18)とを備え、さらに前記電解液槽
(7)に電解液返却管(15)を介して接続されている遠心分
離機(13)と防錆油槽(22)の底部とを返却管(25)により接
続したことを特徴とする電解バリ取り装置。
1. An electrolytic solution supply pipe (6) is connected between the electrolytic solution tank (7) and the electrode (2), and the electrode (2) and the centrifuge are separated.
An electrolyte solution discharge pipe (14) is connected between (13) and a centrifugal separator (13) and the electrolyte solution tank (7) and an electrolyte solution return pipe (15).
Rust preventive oil that supplies rust preventive oil between the electrolytic deburring station (1) connected by the above, the jig (19) for setting the electrolytic deburred work (3) and the rust preventive oil tank (22) Supply pipe (21)
And a rust preventive station (18) connected by a rust preventive oil discharge pipe (24) for returning rust preventive oil between the jig (19) and the rust preventive oil tank (22). Electrolyte tank
An electrolytic burr characterized in that the centrifuge (13) connected to the (7) via the electrolyte return pipe (15) and the bottom of the rust preventive oil tank (22) are connected by the return pipe (25). Taker.
JP17189587U 1987-11-10 1987-11-10 Electrolytic deburring device Expired - Lifetime JPH061299Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17189587U JPH061299Y2 (en) 1987-11-10 1987-11-10 Electrolytic deburring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17189587U JPH061299Y2 (en) 1987-11-10 1987-11-10 Electrolytic deburring device

Publications (2)

Publication Number Publication Date
JPH0179528U JPH0179528U (en) 1989-05-29
JPH061299Y2 true JPH061299Y2 (en) 1994-01-12

Family

ID=31463896

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17189587U Expired - Lifetime JPH061299Y2 (en) 1987-11-10 1987-11-10 Electrolytic deburring device

Country Status (1)

Country Link
JP (1) JPH061299Y2 (en)

Also Published As

Publication number Publication date
JPH0179528U (en) 1989-05-29

Similar Documents

Publication Publication Date Title
US6315885B1 (en) Method and apparatus for electropolishing aided by ultrasonic energy means
WO2017030329A1 (en) System for supplying and circulating recyclable release agent for die casting
EP1445353A1 (en) Method and device for surface treatment of treated object
JPH061299Y2 (en) Electrolytic deburring device
US3945388A (en) Apparatus for counterflow rinsing of workpieces
JP3400780B2 (en) Method and apparatus for performing electrochemical treatment
US3255097A (en) Method and apparatus for clarifying electrolyte
JP3703132B2 (en) Electrochemical treatment method such as electroplating and electrochemical reaction apparatus thereof
JPS6229520B2 (en)
JP4369722B2 (en) Method and apparatus for copper sulfate plating of plate roll
CN213645055U (en) Cleaning machine for cleaning electroplated solder balls
JPH089127B2 (en) Electrolytic deburring device
JP2005029876A (en) Copper sulfate plating method
JP2003039275A (en) Method and apparatus for supplying treating liquid in machine tool
JPH0785848B2 (en) Electrolytic deburring method
JP3339130B2 (en) Chemical cleaning method
JP2000189834A (en) Cleaning liquid purification device and purification method
JPH10180238A (en) Method and apparatus for treating residual ready-mixed concrete
CN211103309U (en) Rust removal equipment for machining
US2381183A (en) Apparatus for and method of rustproofing
JPS63153293A (en) Surface treatment of work
JP2979830B2 (en) Metal scrap cleaning equipment
JP2005334784A (en) Used water recycling equipment
JPH0242613B2 (en)
JPS6244990Y2 (en)