CN201400723Y - Tubular anode - Google Patents

Tubular anode Download PDF

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Publication number
CN201400723Y
CN201400723Y CN2009201071460U CN200920107146U CN201400723Y CN 201400723 Y CN201400723 Y CN 201400723Y CN 2009201071460 U CN2009201071460 U CN 2009201071460U CN 200920107146 U CN200920107146 U CN 200920107146U CN 201400723 Y CN201400723 Y CN 201400723Y
Authority
CN
China
Prior art keywords
electrode
anode
anion
tubular anode
exchange membrane
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
CN2009201071460U
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Chinese (zh)
Inventor
李政雄
何福海
杨楠
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.)
Ande Membrane Separation Technology & Engineering (beijing) Co Ltd
Original Assignee
Ande Membrane Separation Technology & Engineering (beijing) Co Ltd
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 Ande Membrane Separation Technology & Engineering (beijing) Co Ltd filed Critical Ande Membrane Separation Technology & Engineering (beijing) Co Ltd
Priority to CN2009201071460U priority Critical patent/CN201400723Y/en
Application granted granted Critical
Publication of CN201400723Y publication Critical patent/CN201400723Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses a tubular anode belonging to the range of electrophoresis coating device components. An anion-exchange membrane which is adhered in tube shape is sleeved on a polymer framework, the polymer framework is fixedly connected between an anode cap and a cap tail, an electrode is placed inside the polymer framework, the anode cap is covered at the top end of the electrode andis in seal connection with a water outlet pipe via a union joint, and a water inlet pipe is sealed at the bottom end of the electrode through an sealing ring inside the electrode. The tubular anode utilizes the selective and unidirectional anion-exchange membrane to effectively remove organic acid generated during an electrophoresis coating process, reduces corrosion of the electrode and improvesstability of technological parameters.

Description

A kind of tubular anode
Technical field
The utility model belongs to the parts scope of electrophoretic painting device, relates in particular to a kind of tubular anode of the pump circulation of the employing union sealing of being with anion-exchange membrane.
Background technology
Ion-exchange membrane is a kind of functional polymer film of selecting perviousness that has.The film of being made up of anion-exchange material is called anion-exchange membrane, and it has the selection perviousness to negatively charged ion, is called for short cavity block.Ability cathode electrophoresis is the coating process that generally adopts, it is the main means that improve coated article work-ing life (erosion resistance), be widely used in industries such as automobile making, machinery, electrical equipment, five metals, give performances such as the good decoration of workpiece, protection against corrosion and weather.In ability cathode electrophoresis, the electrophoretic paint that is adopted is the resin and the pigment slurry of cationic (positively charged), and coated article is as negative electrode.Initial reaction on negative electrode is that water electrolysis forms hydrogen and hydroxide ion (OH-), this reaction causes cathode surface to produce the high alkalinity interfacial layer, make the aggegation on negative electrode of positively charged particle, positively charged ion (resin and pigment) produces the deposition of filming with hydroxide ion (OH-) reaction.Constantly produce organic acid in the positive column, these acid as untimely removing will make tank liquor pH value descend, and influence the stable of processing parameter, influence throwing power, and the solvability of filming again increases, and the consumption of electrode of positively charged is accelerated simultaneously.
Summary of the invention
The utility model purpose is to provide a kind of tubular anode at the deficiencies in the prior art, by water inlet pipe 1, rising pipe 2, union formula joint 3, anode cap 4, pull bar 5, electrode 6, anion-exchange membrane 7, macromolecular scaffold 8, utmost point inner seal ring 9, cover tail 10 is formed, it is characterized in that, bonding one-tenth piped anion-exchange membrane 7 is enclosed within on the macromolecular scaffold 8, macromolecular scaffold 8 is fixed on anode cap 4 and the cover tail 10, electrode 6 places in the macromolecular scaffold 8, union formula joint 3 is tightly connected anode cap 4 and rising pipe 2, and water inlet pipe 1 is implemented sealing in electrode 6 bottoms by utmost point inner seal ring 9.
Described electrode 6 is by pull bar 5 and power turn-on.
Described anion-exchange membrane is to be made of vinylbenzene quaternary ammonium type anion exchange resin and polyethylene.
The material of described macromolecular scaffold is PP, UPVC or ABS; Endoporus is rectangle or square.
The material of described electrode is through the 316L of transpassivation stainless steel or is coated with ruthenium titanium electrode.
The beneficial effects of the utility model are to use selection type, unidirectional anion-exchange membrane to remove the organic acid that produces in the electrophoretic painting process effectively, have reduced the corrosion of electrode; Realize the processing of electrode solution exit seal by union formula joint, force the anolyte Rapid Cycle, improve the stability of processing parameter.
Description of drawings
Fig. 1 is a tubular anode broken section structure iron.
Embodiment
The utility model provides a kind of tubular anode.Below in conjunction with accompanying drawing the utility model is illustrated.In tubular anode broken section structure iron shown in Figure 1, bonding one-tenth piped anion-exchange membrane 7 is enclosed within on the macromolecular scaffold 8, macromolecular scaffold 8 is fixed on anode cap 4 and the cover tail 10, electrode 6 places in the macromolecular scaffold 8, union formula joint 3 is tightly connected anode cap 4 and rising pipe 2, and water inlet pipe 1 is implemented sealing in electrode 6 bottoms by utmost point inner seal ring 9; Described electrode 6 is by pull bar 5 and power turn-on.
Described anion-exchange membrane 7 is to be made of vinylbenzene quaternary ammonium type anion exchange resin and polyethylene, its intrinsic activity radicals R-CH2N+ (CH3) 3, cause film body to possess the characteristic that the ion selection sees through, use in the effective removal production process in the tank liquor negative ions such as remaining acid group, the penetrating rate of ion is higher than 99.9%.
Described macromolecular scaffold 8 materials can be PP, UPVC or ABS, endoporus is that rectangle or foursquare structure possess intensity preferably, higher porosity, can fine support anion-exchange membrane, make it keep level and smooth and clean and tidy surface, so can not take place to pollute such as wrinkling, cracking, piling thing.
Described electrode 6 materials are through the 316L of transpassivation stainless steel or are coated with ruthenium titanium electrode.Union formula joint 3 is common loose joint forms, and material is UPVC, is easy to processing.Use this joint assembling fast, flexible operation, good airproof performance.
Anode with the automobile cathode electrophoresis painting dressing is an example below, in conjunction with the accompanying drawings and be described further.
In cathode electro-coating, power supply is by pull bar 5 and electrode 6 conductings, electrolytic reaction takes place in the positive column, generate hydrogen ion and oxygen, under the effect of recycle pump, enter into utmost point inner seal ring 9 by water inlet pipe 1 from anolyte, flow through and cover tail 10 back risings, during through macromolecular scaffold 8, negative ions such as acid in the Electrophoretic Paints or solubilizing agent are attracted to take place migration by anode and enter in the anolyte of polymer tube 8 by the anion-exchange membrane 7 of selecting perviousness, the hydrogen ion of electrode surface is combined into acid, and along with the swirling flow of anolyte is moved, arrive anode cap 4 tops and get back to utmost point liquid bath through rising pipe 2, by anolyte pH value in the automatic adjustment utmost point liquid bath, keep the chemical equilibrium of system.Guarantee throwing power and film performance.

Claims (5)

1. tubular anode, it is characterized in that, bonding one-tenth piped anion-exchange membrane (7) is enclosed within on the macromolecular scaffold (8), macromolecular scaffold (8) is fixed between anode cap (4) and the cover tail (10), electrode (6) places in the macromolecular scaffold (8), union formula joint (3) is tightly connected anode cap (4) and rising pipe (2), and water inlet pipe (1) is implemented sealing in electrode (6) bottom by utmost point inner seal ring (9).
2. according to the described tubular anode of claim 1, it is characterized in that described electrode (6) is by pull bar (5) and power turn-on.
3. according to the described tubular anode of claim 1, it is characterized in that described anion-exchange membrane is to be made of vinylbenzene quaternary ammonium type anion exchange resin and polyethylene.
4. according to the described tubular anode of claim 1, it is characterized in that the material of described macromolecular scaffold is PP, UPVC or ABS; Endoporus is rectangle or square.
5. according to the described tubular anode of claim 1, it is characterized in that the material of described electrode is through the 316L of transpassivation stainless steel or is coated with ruthenium titanium electrode.
CN2009201071460U 2009-04-09 2009-04-09 Tubular anode Expired - Lifetime CN201400723Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009201071460U CN201400723Y (en) 2009-04-09 2009-04-09 Tubular anode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009201071460U CN201400723Y (en) 2009-04-09 2009-04-09 Tubular anode

Publications (1)

Publication Number Publication Date
CN201400723Y true CN201400723Y (en) 2010-02-10

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009201071460U Expired - Lifetime CN201400723Y (en) 2009-04-09 2009-04-09 Tubular anode

Country Status (1)

Country Link
CN (1) CN201400723Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105980612A (en) * 2014-02-10 2016-09-28 株式会社荏原制作所 Anode holder and plating device
CN110592643A (en) * 2019-10-23 2019-12-20 湖北澳美斯汽车零部件有限公司 Electrophoresis system for automobile mixed line coating

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105980612A (en) * 2014-02-10 2016-09-28 株式会社荏原制作所 Anode holder and plating device
CN105980612B (en) * 2014-02-10 2018-09-28 株式会社荏原制作所 Anode holder and plater
CN110592643A (en) * 2019-10-23 2019-12-20 湖北澳美斯汽车零部件有限公司 Electrophoresis system for automobile mixed line coating
CN110592643B (en) * 2019-10-23 2021-04-09 湖北澳美斯汽车零部件有限公司 Electrophoresis system for automobile mixed line coating

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CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20100210