JPS6346399B2 - - Google Patents

Info

Publication number
JPS6346399B2
JPS6346399B2 JP23304782A JP23304782A JPS6346399B2 JP S6346399 B2 JPS6346399 B2 JP S6346399B2 JP 23304782 A JP23304782 A JP 23304782A JP 23304782 A JP23304782 A JP 23304782A JP S6346399 B2 JPS6346399 B2 JP S6346399B2
Authority
JP
Japan
Prior art keywords
tube
treated
soft porous
circumferential surface
tubular electrode
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
JP23304782A
Other languages
Japanese (ja)
Other versions
JPS59123000A (en
Inventor
Koji Sakagishi
Mitsuo Hara
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.)
GENSHIRIYOKU DAIKO KK
Original Assignee
GENSHIRIYOKU DAIKO 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 GENSHIRIYOKU DAIKO KK filed Critical GENSHIRIYOKU DAIKO KK
Priority to JP23304782A priority Critical patent/JPS59123000A/en
Publication of JPS59123000A publication Critical patent/JPS59123000A/en
Publication of JPS6346399B2 publication Critical patent/JPS6346399B2/ja
Granted legal-status Critical Current

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  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】 この発明は、管材の外周面の汚染を電解処理に
より除去する管材外周面の汚染電解除去処理装置
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for electrolytically removing contamination from the outer circumferential surface of a tube, which removes contamination from the outer circumferential surface of the tube by electrolytic treatment.

例えば原子力設備で使用した足場用パイプや配
管等の管材で、外周面が汚染している場合、従来
は電解槽内の電解液に、被処理管材を浸漬して付
着物質を除去していたが、長尺の管材を浸漬でき
る電解槽の長さには限度があり、電解槽の長さを
超える長尺管材についてはこれを処理可能な長さ
に切断しなければならないばかりか、多量の電解
液が必要となるなどの点に問題があつた。
For example, if the outer surface of tubing materials such as scaffolding pipes or piping used in nuclear power facilities is contaminated, conventionally the material to be treated is immersed in an electrolytic solution in an electrolytic tank to remove the adhering substances. However, there is a limit to the length of the electrolytic tank in which long pipes can be immersed, and long pipes that exceed the length of the electrolytic tank must be cut to a length that can be processed. There were problems with the need for liquid.

この発明は、上述の問題を解決した管材外周面
の汚染電解除去処理装置を提供するもので、被処
理管材の外径よりも内径を小寸とした軟質多孔材
管を、管状電極内に同心的に支持し、管状電極の
内周面と前記軟質多孔材管の外周面との間を電解
液通路に形成する一方、管状電極の両端部に被処
理管材の外周面しごき用シール部材を取付け、か
つ、前記軟質多孔材管及びシール部材をそれぞれ
交換自在とした点に特徴がある。
The present invention provides an apparatus for electrolytically removing contamination from the outer circumferential surface of a tube material, which solves the above-mentioned problems.A soft porous tube whose inner diameter is smaller than the outer diameter of the tube material to be treated is placed concentrically within a tubular electrode. while forming an electrolyte passageway between the inner circumferential surface of the tubular electrode and the outer circumferential surface of the soft porous material tube, and attaching sealing members for ironing the outer circumferential surface of the tube to be treated to both ends of the tubular electrode. , and is characterized in that the soft porous material tube and the sealing member are each replaceable.

ついで、この発明の装置を実施例により図面を
参照しながら説明する。
Next, the apparatus of the present invention will be explained by way of embodiments with reference to the drawings.

第1図にはこの発明の装置の実施例を縦断側面
図で、また、第2図には正面図で、さらに、第3
図には第1図―線部分の断面図でそれぞれ示
してある。図面に示したように、この発明の装置
は、ポリエチレン発泡体等、スポンジ状の軟質多
孔材管1を管状電極2の内部に同心的に支持して
ある。
FIG. 1 shows an embodiment of the device of the present invention in a longitudinal sectional side view, FIG. 2 shows a front view, and a third
Each figure shows a sectional view taken along the line in FIG. 1. As shown in the drawings, the device of the present invention has a sponge-like soft porous material tube 1, such as polyethylene foam, supported concentrically inside a tubular electrode 2.

軟質多孔材管1は内径を被処理管材3の外径よ
りも小寸としてあり、管状電極2の内周面と軟質
多孔材管1の外周面との間を環状の電解液通路4
に形成してある。
The soft porous material tube 1 has an inner diameter smaller than the outer diameter of the tube material 3 to be treated, and an annular electrolyte passage 4 is provided between the inner circumferential surface of the tubular electrode 2 and the outer circumferential surface of the soft porous material tube 1.
It is formed in

一方、管状電極2は両端にフランジ5,5を有
する。
On the other hand, the tubular electrode 2 has flanges 5, 5 at both ends.

フランジ5,5は双方ともフランジ本体5Aに
環状板5B,5Cを重ねる三層構造とし、フラン
ジ本体5Aと環状板5Bとの間及び、環状板5
B,5Cの間に、それぞれ環状板のゴムまたはプ
ラスチツク製で弾撥的復帰力に富む被処理管材外
周面しごき用シール部材6を挟み、ボルト7とナ
ツト8により緊締してある。この場合必要に応じ
てフランジ5,5を4重以上の構造とし、それぞ
れの間にシール部材6を挟む構造としてもよい。
Both flanges 5 and 5 have a three-layer structure in which annular plates 5B and 5C are stacked on a flange main body 5A, and between the flange main body 5A and annular plate 5B, and the annular plate 5
Between B and 5C, an annular plate made of rubber or plastic and having a strong elastic return force, a sealing member 6 for ironing the outer circumferential surface of the tube to be treated is sandwiched, and tightened with bolts 7 and nuts 8. In this case, if necessary, the flanges 5, 5 may have a structure of four or more layers, and the seal member 6 may be sandwiched between each of the flanges 5, 5.

前記軟質多孔材管1はフランジ本体5A,5A
の基部内側に形成した周溝9,9にそれぞれ嵌着
する可撓材製シールリング10,10により支持
してある。
The soft porous material pipe 1 has flange bodies 5A, 5A.
It is supported by seal rings 10, 10 made of flexible material that fit into circumferential grooves 9, 9 formed inside the base of the holder, respectively.

また、管状電極2には電解液入口11と電解液
出口12及びマイナス側となる端子13を設けて
ある。
Further, the tubular electrode 2 is provided with an electrolyte inlet 11, an electrolyte outlet 12, and a terminal 13 on the negative side.

上述の構成としたこの発明の装置は、電解液入
口11から電解液出口12に向けて所要量の電解
液を流しつつ、管状電極2の端子にマイナス側を
接続し、被処理管材3にプラス側を接続して所定
の電圧を印加するとともに第1図中に矢印で示す
ように被処理管材3をシール部材6の孔を押拡げ
ながら挿入してゆき、軟質多孔材管1を押拡げつ
つ徐々に被処理管材3を前進させてゆくと、被処
理管材3の外周面に軟質多孔材管1の内周面が摺
接し、軟質多孔材管1に含浸している電解液が被
処理管材3の外周面と反応し、電解研磨による汚
染除去が行なわれる。この場合、軟質多孔材管1
とシール部材6は被処理管材3に見合つた最適の
サイズのものと交換しておく。
The apparatus of the present invention configured as described above connects the negative side to the terminal of the tubular electrode 2 while flowing the required amount of electrolyte from the electrolyte inlet 11 toward the electrolyte outlet 12, and connects the negative side to the terminal of the tubular electrode 3 to be treated. While connecting the sides and applying a predetermined voltage, the tube material 3 to be treated is inserted into the hole of the sealing member 6 while pushing it outward as shown by the arrow in FIG. As the tube material 3 to be treated is gradually advanced, the inner circumferential surface of the soft porous tube 1 comes into sliding contact with the outer circumferential surface of the tube material 3 to be treated, and the electrolytic solution impregnated in the soft porous tube 1 flows into the tube material to be treated. It reacts with the outer peripheral surface of No. 3, and the contamination is removed by electrolytic polishing. In this case, the soft porous material pipe 1
The seal member 6 and the seal member 6 are replaced with one of the optimum size suitable for the pipe material 3 to be treated.

軟質多孔材管1内面に摺接して通過した被処理
管材3の部分は、管状電極2の他端部にあるシー
ル部材6,6の孔を押拡げるようにして通過し、
付着している電解液や残留している汚染物質がし
ごき落される。
The portion of the tube material 3 to be treated that has passed through in sliding contact with the inner surface of the soft porous material tube 1 passes through the holes of the sealing members 6, 6 at the other end of the tubular electrode 2 in such a manner as to expand them,
Adhering electrolyte and remaining contaminants are scrubbed off.

なお、間隔をおいて取付けたシール部材6,6
間に、しごき落された電解液や汚染物質を吸水吸
着する材料を介在させたり、あるいは真空吸引す
る機構を設けておくなどすると汚染除去処理はさ
らに高能率となる。
In addition, the seal members 6, 6 attached at intervals
If a material that absorbs and adsorbs the strained electrolyte and contaminants is interposed between them, or if a vacuum suction mechanism is provided, the efficiency of the contamination removal process will be further increased.

電解液は電解液通路4を流れるが、この間に軟
質多孔材管1に十分含浸し、軟質多孔材管1内を
外周面がこすられながら通り抜ける被処理管材3
に確実に接触するものの無駄に流れることは全く
ない。
The electrolyte flows through the electrolyte passage 4, during which time it sufficiently impregnates the soft porous material tube 1, and the treated tube material 3 passes through the soft porous material tube 1 while its outer peripheral surface is rubbed.
Although it definitely comes into contact with the water, it does not flow unnecessarily.

いま、図示されるこの発明の装置において、 被処理管材:外径48.6mm×長さ2400mm×肉厚
2.4mmの寸法を有する鋼材(SS41)、 軟質多孔材管:内径45mm×長さ10mm×肉厚10mm
の寸法を有するポリエチレン発泡体、 シール部材:内径45mm×外径150mm×厚さ2mm
の寸法を有するゴム材、 とし、かつ 被処理管材の送り速度:10cm/min、 電解液:40%りん酸水溶液、 電解液供給量:1000ml/min 被処理管材への印加電圧:8V の条件で実施したところ、処理前の管材では1×
10-5マイクロキユーリー/cm2が測定されたのに対
して、処理後においては全く反応を示さず、完全
に清浄化されていることが確認された。
Now, in the illustrated apparatus of the present invention, pipe material to be treated: outer diameter 48.6 mm x length 2400 mm x wall thickness
Steel material (SS41) with dimensions of 2.4 mm, soft porous pipe: inner diameter 45 mm x length 10 mm x wall thickness 10 mm
Polyethylene foam with dimensions: Seal member: inner diameter 45mm x outer diameter 150mm x thickness 2mm
A rubber material with the dimensions of, and Feeding speed of the tube to be treated: 10 cm/min, Electrolyte: 40% phosphoric acid aqueous solution, Electrolyte supply rate: 1000 ml/min, Voltage applied to the tube to be treated: 8 V. When carried out, it was found that the pipe material before treatment was 1×
Although 10 -5 microcuries/cm 2 was measured, no reaction was observed after treatment, confirming complete cleaning.

以上の説明から明らかなように、この発明の装
置によれば、管材外周面の汚染を確実に除去処理
でき、特に管材がいかに長尺であつても、これを
切断することなく処理できるのは勿論のこと、電
解液は循環使用されるので少量ですみ、経済的で
あるなど工業上有用な効果がもたらされるのであ
る。
As is clear from the above description, the apparatus of the present invention can reliably remove contamination from the outer surface of the pipe material, and in particular can treat the pipe material without cutting it, no matter how long it is. Needless to say, since the electrolytic solution is used repeatedly, only a small amount is required, which brings about industrially useful effects such as being economical.

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

第1図はこの発明の装置の実施例を示す縦断側
面図、第2図は同正面図、第3図は第1図―
線部分の縦断面図である。図面において、 1…軟質多孔材管、2…管状電極、3…被処理
管材、4…電解液通路、5…フランジ、6…シー
ル部材、11…電解液入口、12…電解液出口。
Fig. 1 is a vertical sectional side view showing an embodiment of the device of the present invention, Fig. 2 is a front view of the same, and Fig. 3 is the same as Fig. 1.
It is a longitudinal cross-sectional view of a line part. In the drawings, 1... Soft porous material tube, 2... Tubular electrode, 3... Tube material to be treated, 4... Electrolyte passageway, 5... Flange, 6... Seal member, 11... Electrolyte solution inlet, 12... Electrolyte solution outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 被処理管材の外径よりも内径を小寸とした軟
質多孔材管を、管状電極内に同心的に支持し、管
状電極の内周面と前記軟質多孔材管の外周面との
間を電解液通路に形成する一方、管状電極の両端
部に被処理管材の外周面しごき用シール部材を取
付け、かつ、前記軟質多孔材管及びシール部材を
それぞれ交換自在としたことを特徴とする管材外
周面の汚染電解除去処理装置。
1 A soft porous material tube whose inner diameter is smaller than the outer diameter of the tube material to be treated is concentrically supported within a tubular electrode, and a gap between the inner circumferential surface of the tubular electrode and the outer circumferential surface of the soft porous material tube is An outer periphery of a tubular material formed in an electrolytic solution passageway, characterized in that a sealing member for ironing the outer periphery of the tubular material to be treated is attached to both ends of the tubular electrode, and the soft porous material tube and the sealing member are each replaceable. Surface contamination electrolytic removal treatment equipment.
JP23304782A 1982-12-28 1982-12-28 Electrolytic decontamination device for outer face of pipe Granted JPS59123000A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23304782A JPS59123000A (en) 1982-12-28 1982-12-28 Electrolytic decontamination device for outer face of pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23304782A JPS59123000A (en) 1982-12-28 1982-12-28 Electrolytic decontamination device for outer face of pipe

Publications (2)

Publication Number Publication Date
JPS59123000A JPS59123000A (en) 1984-07-16
JPS6346399B2 true JPS6346399B2 (en) 1988-09-14

Family

ID=16948962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23304782A Granted JPS59123000A (en) 1982-12-28 1982-12-28 Electrolytic decontamination device for outer face of pipe

Country Status (1)

Country Link
JP (1) JPS59123000A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61207600A (en) * 1985-03-11 1986-09-13 Kurinatsupu Kk Electrolytic descaling agent and descaling method for stainless steel

Also Published As

Publication number Publication date
JPS59123000A (en) 1984-07-16

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