JPH0648478Y2 - Structure of Electrolytic Dyeing Section for Electrolytic Dyeing Equipment - Google Patents
Structure of Electrolytic Dyeing Section for Electrolytic Dyeing EquipmentInfo
- Publication number
- JPH0648478Y2 JPH0648478Y2 JP10327987U JP10327987U JPH0648478Y2 JP H0648478 Y2 JPH0648478 Y2 JP H0648478Y2 JP 10327987 U JP10327987 U JP 10327987U JP 10327987 U JP10327987 U JP 10327987U JP H0648478 Y2 JPH0648478 Y2 JP H0648478Y2
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- JP
- Japan
- Prior art keywords
- container
- electrolytic solution
- cathode
- decontamination
- pad
- Prior art date
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Description
【考案の詳細な説明】 (関連産業分野) 本考案は原子力施設に於て、各種物品、移動の困難な大
規模物品、施設の壁面等の金属表面を、電解液が漏洩す
ることなく、且つ又接触面を移動しつつ電解除染を行う
ことのできる電解除染装置用電解除染部の構造に関する
ものである。[Detailed Description of the Invention] (Related industry field) The present invention is used in a nuclear facility without leaking electrolyte solution on various articles, large-scale articles that are difficult to move, metal surfaces such as facility walls, and The present invention also relates to the structure of the electro-dyeing section for the electro-dyeing device capable of performing electro-dyeing while moving the contact surface.
(従来技術) 原子力施設では、放射性物質による汚染の蓄積による高
線量化の防止と、不要品の一時保管および管理区域外へ
の搬出等を目的として金属表面の除染作業を行う。(Prior Art) Nuclear facilities perform decontamination work on metal surfaces for the purpose of preventing an increase in dose due to the accumulation of radioactive substance contamination, temporary storage of unwanted materials, and carrying them out of the controlled area.
現在、多くの除染法が提案されているが、その中でも電
解除染法は迅速・確実・簡便な方法として利用されてい
る。しかし、物品を電解液中に浸し、通電ぢ、陽極溶解
により除染を行うため、電解液槽に浸漬することが出来
る寸法形状の物のみを対象とすることとなり、移動困難
な大型物品および施設の壁面等は電解研磨除染法では不
向きと考えられている。At present, many decontamination methods have been proposed, and among them, the electro-deletion method is used as a quick, reliable, and simple method. However, since articles are soaked in an electrolytic solution and decontamination is carried out by applying electricity and anodic dissolution, only objects of a size and shape that can be immersed in an electrolytic solution tank are targeted, and large articles and facilities that are difficult to move. It is considered that the wall surface and the like are not suitable for the electrolytic polishing decontamination method.
一方、電解液を流しながら陰極を移動しつつ電解研磨除
染を行う現場型接触法が一部で行われているが、電解液
を垂れ流しとするため、床面で電解液を回収しなければ
ならず、使用する電解液量が多くなるばかりでなく、電
解液の回収に困難を強いられている。また電解液の飛散
により、汚染の拡大を招くなどの理由から、一般工業界
で金属表面の鏡面仕上げ用として使用されている他は除
染への適用例は少ない。On the other hand, there are some in-situ contact methods that perform electrolytic polishing decontamination while moving the cathode while flowing the electrolytic solution, but since the electrolytic solution is run off, the electrolytic solution must be collected on the floor surface. In addition, not only the amount of the electrolytic solution to be used is increased, but also the recovery of the electrolytic solution is difficult. In addition, since it is used for the mirror finishing of the metal surface in the general industry, it is rarely applied to decontamination because it causes the spread of pollution due to the scattering of the electrolytic solution.
このため、電解液を除染と同時に回収、循環処理を行う
事を前提とした、除染対象金属表面を容易に移動出来る
現場向けの電解研磨除染用装置の提案が強く要望されて
いる。Therefore, it is strongly desired to propose an electrolytic polishing decontamination apparatus for a site, which is capable of easily moving the surface of the metal to be decontaminated, on the assumption that the electrolytic solution is collected and circulated at the same time as the decontamination.
この要望に応えるものとして、本出願人は先に「現場用
電解除染装置」と題する発明を開示した(特開昭62−11
6299号公報)。これは金属表面に接触し、電解液を保持
することにより除染を行う除染部と、電解液を吸引及び
濾過処理を行ない、容器内へ電解液を吐出させることが
可能な循環系とからなり、除染部は電解液の吸引口を有
する内容器と、同様に電解液の吸引口を有し外周に空気
取入口を具えた外容器と、電解液を吐出する複数個の吐
出孔を有する陰極及びパッドを具えた陰極容器とからな
り、又循環系は内容器と外容器から電解液を吸引し、電
解液タンクに頂溜し、濾過器を通じて連続的に陰極内へ
向け循環されるようにしたものである。In order to meet this demand, the present applicant has previously disclosed an invention entitled "On-site electro-dyeing device" (Japanese Patent Laid-Open No. 62-11).
6299 publication). This consists of a decontamination part that contacts the metal surface and performs decontamination by holding the electrolytic solution, and a circulation system that can perform electrolytic solution suction and filtration processing and discharge the electrolytic solution into the container. The decontamination section includes an inner container having an electrolyte solution suction port, an outer container having an electrolyte solution suction port similarly having an air inlet on the outer periphery, and a plurality of discharge holes for discharging the electrolyte solution. It has a cathode container having a cathode and a pad, and the circulation system sucks the electrolytic solution from the inner container and the outer container, collects the electrolytic solution in the electrolytic solution tank, and circulates continuously through the filter into the cathode. It was done like this.
しかし、これの除染部は循環する電解液が陰極容器の吐
出孔から吐出されてパッド内に保持され、内容器と外容
器の両方から回収されるようになっており、又外容器の
空気取入口から適量の空気を容器内に取入れることによ
って、容器内の負圧の過度の上昇を防止して除染装置が
吸い着くのを防ぎスムーズに除染装置が動くようになっ
ていて、所期の効果を発揮するものであるが、除染部の
構成が複雑となること、狭くて凹凸のある除染面への適
用がいまひとつ不十分である等の問題があった。However, in the decontamination part, the circulating electrolytic solution is discharged from the discharge hole of the cathode container and held in the pad, and is collected from both the inner container and the outer container. By introducing an appropriate amount of air into the container from the intake port, it is possible to prevent the negative pressure in the container from rising excessively and prevent the decontamination device from sticking to it, allowing the decontamination device to move smoothly. Although the desired effect is exhibited, there are problems that the structure of the decontamination part is complicated, and that the application to the decontamination surface having a narrow and uneven surface is insufficient.
(考案により解決しようとする問題点) 上記先願の問題点を解決し除染部の構成をより簡単化
し、狭い部分への適用はもとより、凹凸面への適用の容
易な電解除染装置を提供しようとするものである。(Problems to be solved by devising) The problems of the above-mentioned prior application were solved to simplify the constitution of the decontamination part, and to apply the electro-deletion dyeing device which can be applied not only to a narrow part but also to an uneven surface. It is the one we are trying to provide.
(考案による解決手段) 先端に複数個の電解液吐出用孔を有する陰極容器と、該
陰極容器を囲繞し先端開放部が前記陰極容器との間に吸
込隙間をもって同心状に配設され吸込管を備えた外容器
と、該外容器の先端開放部を覆い、外容器の側胴部に締
着したパッドとで電解除染装置用電解除染部を構成し
た。(Solution by the Invention) A cathode container having a plurality of electrolyte discharge holes at its tip, and a suction tube in which the cathode container is surrounded and a tip opening portion is concentrically provided with a suction gap between the cathode container and the cathode container. The outer container provided with the outer container and the pad that covers the open end portion of the outer container and is fastened to the side body of the outer container constitute the electro-dyeing section for the electro-dyeing apparatus.
(実施例) 第1図において、Aは本考案に係る電解除染部である。
Bは電解除染部A内へ電解液を吐出・回収を行う循環系
(以下単に循環系という)である。Cは循環系Bと電解
除染部Aを結ぶフレキシブルチューブである。電解液
は、ポンプ1により濾過器2を通って電解除染部Aに送
り込まれる。バルブV6は濾過器2のドレンバルブであ
る。バルブV1,V2は電解液の流量調整を行ない、流量計
3によって流量を知る事が出来る。電解液は濾過器2に
よってスラッジ等を除去される。(Embodiment) In FIG. 1, A is an electrolysis dyeing unit according to the present invention.
B is a circulation system (hereinafter, simply referred to as a circulation system) that discharges and collects the electrolytic solution into the electrolysis dyeing section A. C is a flexible tube that connects the circulation system B and the electrolysis dyeing unit A. The electrolytic solution is sent by the pump 1 through the filter 2 to the electrolysis-dyeing section A. The valve V 6 is the drain valve of the filter 2. The valves V 1 and V 2 adjust the flow rate of the electrolytic solution, and the flow rate can be known by the flow meter 3. Sludge and the like is removed from the electrolytic solution by the filter 2.
電解除染部A内へ吐出された電解液は陰極となる陰極容
器4と、陽極となる被除染物5との間に電気を流すこと
により、被除染物5の表面の陽極電解を行なう。こゝ
で、陽極ケーブル6(第1図)は被除染物5に陽極位を
与えるケーブルであり、陰極ケーブル7は陰極容器4に
陰極位を与えるものである。The electrolysis solution discharged into the electro-deletion dyeing section A conducts anodic electrolysis on the surface of the decontamination target 5 by passing electricity between the cathode container 4 serving as a cathode and the decontamination target 5 serving as an anode. Here, the anode cable 6 (FIG. 1) is a cable that gives the object to be decontaminated 5 an anode position, and the cathode cable 7 gives the cathode container 4 a cathode position.
陰極容器4にはその先端に複数個の電解液吐出用孔4bが
あいており、この孔を通して電解液が吐出される。8は
パッドで被除染物5と陰極容器4との間の空間に取り付
けられている。パッド8は電解液を均一に保持する役割
を持っている。The cathode container 4 has a plurality of electrolyte solution discharge holes 4b at its tip, through which the electrolyte solution is discharged. Reference numeral 8 denotes a pad which is attached to the space between the article to be decontaminated 5 and the cathode container 4. The pad 8 has a role of uniformly holding the electrolytic solution.
次に電解除染部Aについて説明する。電解除染部Aは前
に述べた如く陰極容器4と外容器9及びパッド8から構
成される。陰極容器4は電解液を導入する導管部4aと、
該導管部4aの先端にあって、電解液を吐出する複数の吐
出用孔4bを備えた大径部4cからなっている。Next, the electro-dyeing section A will be described. The electro-deletion section A comprises the cathode container 4, the outer container 9 and the pad 8 as described above. The cathode container 4 has a conduit portion 4a for introducing an electrolytic solution,
At the tip of the conduit portion 4a, a large diameter portion 4c having a plurality of discharge holes 4b for discharging an electrolytic solution is formed.
9は陰極容器4の外側を囲む外容器で、空気と電解液を
吸引する吸引管10を側胴部に備えている。外容器9の先
端部は前記陰極容器4の大径部4cとの間に環状の吸込用
隙間11を有している。外容器9の先端部にはパッド8が
被覆され、これはパッド固定具12によって外容器9の側
胴部に締着されている。パッド8は第4図に示す如く電
解液の保持および通過性を持たせるためにノズル開口部
巾W(第2図)の1/5〜1/20の程度の厚みtを持ったス
ポンジ状の耐酸性樹脂繊維(たとえばポリエステル樹
脂)8aと、パッドの液保持量と耐久性を増すための耐酸
性布8bとの2重構造となっており、外容器9の開口面を
完全に覆っている。Reference numeral 9 denotes an outer container that surrounds the outside of the cathode container 4, and is provided with a suction tube 10 for sucking air and an electrolytic solution in the side body portion. The tip of the outer container 9 has an annular suction gap 11 between it and the large diameter portion 4c of the cathode container 4. The tip of the outer container 9 is covered with a pad 8, which is fastened to the side body of the outer container 9 by a pad fixing tool 12. As shown in FIG. 4, the pad 8 has a sponge-like shape having a thickness t of about 1/5 to 1/20 of the nozzle opening width W (FIG. 2) in order to retain and pass electrolyte. It has a double structure of an acid resistant resin fiber (for example, polyester resin) 8a and an acid resistant cloth 8b for increasing the liquid holding amount and durability of the pad, and completely covers the opening surface of the outer container 9. .
外容器9は陰極容器4の導管部4aにたとえばねじ結合さ
れて一体となっている。13は外容器の上部にあって陰極
容器4に取付けられた端子台で、該端子台に端子14を介
し陰極ケーブル7が接続されている。The outer container 9 is integrated with the conduit portion 4a of the cathode container 4 by, for example, screwing. Reference numeral 13 denotes a terminal block attached to the cathode container 4 at the upper part of the outer container, and the cathode cable 7 is connected to the terminal block via the terminal 14.
本発明は以上説明した如く、電解除染装置の除染部の構
造に関するものであるが、電極の極性を逆にすればメッ
キ装置としても応用することができる。As described above, the present invention relates to the structure of the decontamination part of the electro-deletion dyeing device, but it can also be applied as a plating device if the polarities of the electrodes are reversed.
(作用) フレキシブルチユーブCから送られた電解液は陰極容器
4の導管部4aから同じく大径部4cに溜り、吐出用孔4bか
らパッド8内に吐出され、パッド8を湿潤させる。そし
てノズルが被除染物5に接していない場合は、パッド8
を浸潤している電解液は環状の吸引用隙間11から吸引管
10より速やかに回収される。このため電解液のノズル外
への漏洩は起らない。(Function) The electrolytic solution sent from the flexible tube C collects from the conduit portion 4a of the cathode container 4 to the large diameter portion 4c, is discharged from the discharging hole 4b into the pad 8, and wets the pad 8. If the nozzle is not in contact with the material to be decontaminated 5, the pad 8
The electrolyte infiltrating the electrolyte is sucked from the suction gap 11
Recovered faster than 10. Therefore, the electrolyte does not leak out of the nozzle.
実際に除染を行う場合には、電解除染部Aを被除染物5
に対して面圧を加えて接触させると、電解除染部Aは被
除染物5に対してパッド8を介して密着するため陰極部
先端での液吸引は起きず、液保持力は増大する。そして
陽極溶解に必要とする充分な液量を確保でき、陰極容器
4に電流を印加することにより電解除染が行われる。When actually performing decontamination, the electro-deletion dyeing part A is to be decontaminated 5
When a surface pressure is applied to the electrode 5 to bring it into contact with the object to be decontaminated 5 through the pad 8, the liquid is not sucked at the tip of the cathode part and the liquid holding power is increased. . Then, a sufficient amount of liquid required for anodic dissolution can be secured, and by applying an electric current to the cathode container 4, electrolysis dyeing is performed.
更に、陽極溶解を終えた電解液は空気と陽極溶解時に発
生したガスと共に、陰極容器4と外容器9との間の吸込
用隙間11から回収される。この場合、実質的な吸引部分
の面積は少なくなり、パッド8の周辺から吸い込まれる
空気の流速が速くなって、より速やかに電解液が回収さ
れるため、除染時においても液の漏洩は起こらない。Further, the electrolytic solution which has been dissolved in the anode is collected from the suction gap 11 between the cathode container 4 and the outer container 9 together with air and the gas generated during the dissolution of the anode. In this case, the substantial area of the suction portion is reduced, the flow velocity of the air sucked from the periphery of the pad 8 is increased, and the electrolytic solution is recovered more quickly, so that the liquid does not leak even during decontamination. Absent.
このように、パッド8の厚みにより吸込用隙間11と被除
染物5の間に空気を通過させる間隙が保てるため、吸引
により生じた陰圧で電解除染部Aの先端が被除染物5に
吸着することなく、被除染物5の面上を自由に移動しな
がら除染を行うことができる。In this way, since the thickness of the pad 8 allows a space for allowing air to pass between the suction gap 11 and the substance to be decontaminated 5, the negative pressure generated by the suction causes the tip of the electro-deletion portion A to reach the substance to be decontaminated 5. It is possible to perform decontamination while freely moving on the surface of the article to be decontaminated 5 without adsorbing.
さらに、電解時の熱の発生に関しては、大量の空気と共
に電解液が吸引されるので厚くなった電解液は速やかに
冷却され、熱の蓄積は少なくなる。このため、電極に対
する電流密度を従来の除染部より高くなる事が可能とな
った。Further, regarding the generation of heat during electrolysis, since the electrolytic solution is sucked together with a large amount of air, the thickened electrolytic solution is quickly cooled and the heat accumulation is reduced. Therefore, the current density for the electrode can be made higher than that of the conventional decontamination part.
陽極電解を終えた電解液・空気・発生ガスはフレキシブ
ルチユーブCを通って電解液タンク15へ吸引される。電
解液タンク15に回収された電解液は再び循環使用され
る。16は液面計で、これにより液タンク15の電解流量の
監視をする。The electrolytic solution / air / generated gas that has undergone the anode electrolysis passes through the flexible tube C and is sucked into the electrolytic solution tank 15. The electrolyte solution collected in the electrolyte solution tank 15 is recycled again. A liquid level gauge 16 monitors the electrolytic flow rate of the liquid tank 15.
液タンク15内で分離された空気及びガスは排風機19で排
出されるが、ミストトラップ17でミストが、又排気フイ
ルタ18で塵埃等が取り除かれる。排風機19は電解液タン
ク15を負圧にし、陽極電解を終えた電解液を回収すると
共に、回収した空気及びガスを吸引排気する2つの役割
を持っている。20は直流電源、21はポンプ流量制御用の
インバータである。The air and gas separated in the liquid tank 15 are exhausted by the exhaust fan 19, but the mist is removed by the mist trap 17 and the dust is removed by the exhaust filter 18. The exhaust fan 19 has two functions of making the electrolytic solution tank 15 a negative pressure, collecting the electrolytic solution which has completed the anode electrolysis, and sucking and exhausting the collected air and gas. 20 is a DC power supply, and 21 is an inverter for controlling the pump flow rate.
(効果) 1)電解液は大量の空気と共に吸引され、速やかに冷却
されるので熱の発生が少なく、電極に対する電流密度を
従来の現場型接触法より高くして陽極溶解量を増すこと
ができる。(Effect) 1) The electrolytic solution is sucked together with a large amount of air and cooled rapidly, so that less heat is generated, and the current density for the electrode can be made higher than that of the conventional in-situ contact method to increase the amount of anodic dissolution. .
2)吐出した電解液を回収するための受皿を必要としな
いため、大型、且つ据え置きされた構造物の除染が出来
る。2) Since a tray for collecting the discharged electrolytic solution is not required, it is possible to decontaminate a large and stationary structure.
3)電解液の垂れ流しが無いため、除染対象物以外の設
備、機器等への影響が少ない。3) Since there is no drainage of the electrolytic solution, there is little effect on facilities and equipment other than the decontamination target.
4)電解液を直接吸引回収し循環使用するので、電解液
量が少なくて済み、装置の小型化をはかれる。4) Since the electrolytic solution is directly sucked and collected and circulated for use, the amount of the electrolytic solution can be small and the apparatus can be downsized.
5)使用電流が浸漬法に比べ格段に少ないためランニン
グコストの低減がはかれる。5) Since the current used is much smaller than that of the immersion method, the running cost can be reduced.
6)小型軽量のためマニプレータ等によって操作が出
来、放射性物質取扱施設のセル内等の立ち入り不可能場
所での除染に有効である。6) Since it is small and lightweight, it can be operated by a manipulator, etc., and is effective for decontamination in places where access is not possible, such as in cells of radioactive material handling facilities.
7)各種形状(平面、曲面、突起部分等)、および寸法
(小物物品から大型構造物まで)の対象物の除染が可能
であり適用範囲が広い。7) It is possible to decontaminate objects of various shapes (flat surfaces, curved surfaces, protrusions, etc.) and dimensions (from small articles to large structures), and its application range is wide.
8)陽極溶解とパッドの物理的研磨力との相乗効果によ
り除染効果が高い。8) The decontamination effect is high due to the synergistic effect of the anodic dissolution and the physical polishing power of the pad.
第1図は本考案に係る電解除染部を使用した全体説明
図。 第2図は電解除染部の縦断面図、パッドが被除染物に接
触していない状態を示す。 第3図は第2図のIII−III断面図。 第4図はパッドの断面図。 第5図は第2図と同様図面で、除染時の状態を示す。 図において; A……電解除染部、B……循環系 C……フレキシブルチューブ 1……電解液循環ポンプ、2……濾過器 3……流量計、4……陰極容器 4a……導管部、4b……吐出用孔 4c……大径部、4d……陰極面 5……被除染物、6……陽極ケーブル 7……陰極ケーブル、8……パッド 8a……耐酸性樹脂繊維、8b……耐酸性布 9……外容器、10……吸引管 11……吸込用環状隙間、12……パッド固定具 13……端子台、14……端子 15……電解液タンク、16……液面計 17……ミストトラップ、18……排気フイルタ 19……排風機、20……直流電源 21……インバータ、22……電解液回収ポンプ V1……流量調整用バイパスバルブ V2……流量調整用バルブ V3……電解液回収ポンプバルブ V4……負圧調整バルブ、V5……ドレンバルブ V6……ドレンバルブ、V7……吐出停止バルブ V8……電解液回収ポンプ用バイパスバルブFIG. 1 is an overall explanatory view using the electro-dyeing section according to the present invention. FIG. 2 is a vertical cross-sectional view of the electro-deletion dyeing section, showing a state where the pad is not in contact with the article to be decontaminated. FIG. 3 is a sectional view taken along the line III-III in FIG. FIG. 4 is a sectional view of the pad. FIG. 5 is a drawing similar to FIG. 2 and shows the state during decontamination. In the figure: A ... Electrolytic dyeing section, B ... Circulation system C ... Flexible tube 1 ... Electrolyte circulation pump, 2 ... Filter 3 ... Flowmeter, 4 ... Cathode container 4a ... Conduit section , 4b ...... Discharge hole 4c ...... Large diameter part, 4d ...... Cathode surface 5 ...... Decontamination object, 6 ...... Anode cable 7 ...... Cathode cable, 8 ...... Pad 8a ...... Acid resistant resin fiber, 8b …… Acid resistant cloth 9 …… Outer container, 10 …… Suction tube 11 …… Suction annular gap, 12 …… Pad fixture 13 …… Terminal block, 14 …… Terminal 15 …… Electrolyte tank, 16 …… Liquid level gauge 17 …… Mist trap, 18 …… Exhaust filter 19 …… Ventilator, 20 …… DC power supply 21 …… Inverter, 22 …… Electrolyte recovery pump V 1 …… Bypass valve for flow adjustment V 2 …… flow regulating valve V 3 ...... electrolyte recovery pump valve V 4 ...... negative pressure regulating valve, V 5 ...... drain valve V 6 ...... drain valve, V 7 Bypass valve for ... a discharge stop valve V 8 ...... electrolyte recovery pump
───────────────────────────────────────────────────── フロントページの続き (72)考案者 中島 順 茨城県那珂郡東海村大字村松161−2 株 式会社原子力代行東海事業所内 (56)参考文献 特開 昭62−116299(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Jun Nakajima 161-2 Muramatsu, Tokai-mura, Naka-gun, Ibaraki Prefecture Inside the Tokai Works, Nuclear Power Agency (56) Reference JP 62-116299 (JP, A)
Claims (1)
する陰極容器(4)と、該陰極容器(4)を囲繞し先端
開放部が前記陰極容器(4)との間に吸込用隙間(11)
をもって同心状に配設された吸込管(10)を備えた外容
器(9)と、該外容器(9)の先端開放部を覆い、外容
器(9)の側胴部に締着したパッド(8)とからなる電
解除染装置用電解除染部の構造。1. A cathode container (4) having a plurality of electrolyte solution discharge holes (4b) at its tip, and a cathode container (4) which surrounds the cathode container (4) and has a tip opening portion between the cathode container (4). Suction gap (11)
Outer container (9) provided with a suction pipe (10) arranged concentrically with each other, and a pad which covers the open end of the outer container (9) and is fastened to the side body of the outer container (9). (8) The structure of the electro-dyeing section for the electro-dyeing device comprising
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10327987U JPH0648478Y2 (en) | 1987-07-07 | 1987-07-07 | Structure of Electrolytic Dyeing Section for Electrolytic Dyeing Equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10327987U JPH0648478Y2 (en) | 1987-07-07 | 1987-07-07 | Structure of Electrolytic Dyeing Section for Electrolytic Dyeing Equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS648695U JPS648695U (en) | 1989-01-18 |
| JPH0648478Y2 true JPH0648478Y2 (en) | 1994-12-12 |
Family
ID=31333963
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10327987U Expired - Lifetime JPH0648478Y2 (en) | 1987-07-07 | 1987-07-07 | Structure of Electrolytic Dyeing Section for Electrolytic Dyeing Equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0648478Y2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019155513A (en) * | 2018-03-09 | 2019-09-19 | 日立造船株式会社 | Electrolytic processing device |
| GB201909090D0 (en) * | 2019-06-25 | 2019-08-07 | C Tech Innovation Ltd | Electrochemical surface treatment |
-
1987
- 1987-07-07 JP JP10327987U patent/JPH0648478Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS648695U (en) | 1989-01-18 |
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