CN203754838U - Steel wire electrolysis phosphating device - Google Patents
Steel wire electrolysis phosphating device Download PDFInfo
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- CN203754838U CN203754838U CN201320851510.0U CN201320851510U CN203754838U CN 203754838 U CN203754838 U CN 203754838U CN 201320851510 U CN201320851510 U CN 201320851510U CN 203754838 U CN203754838 U CN 203754838U
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- phosphating
- saponification
- electrolytic
- solution
- treatment
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Abstract
The utility model discloses a steel wire electrolysis phosphating device. The steel wire electrolysis phosphating device comprises an electrolytic solution treatment system, an electrolysis phosphating system, a saponification protecting treatment system and a drying treatment system, into which steel wires subjected to thermal treatment are sequentially input, wherein the electrolytic solution treatment system comprises an electrode I, an electrolytic solution tank, a solution storage tank and a solution feed pump; the electrolysis phosphating system comprises an electrode II, a phosphating tank, a phosphating solution pump and a phosphating solution tank; the saponification protecting treatment system comprises a saponification solution tank, a saponification solution pump and a saponification solution storage tank; the drying treatment system comprises a drying device and a drying device heating device. The steel wires subjected to thermal treatment are input into the electrolysis phosphating device and are subjected to electrolytic solution treatment, electrolysis phosphating treatment, saponification protecting treatment and drying treatment, so that little oxide remaining on the surfaces of the steel wires is quickly eliminated under the effect of ionization; phosphating layers on the surfaces are fully protected through saponification; the pollution problem is reduced by drying a saponification solution on the surfaces of the steel wires.
Description
Technical field
The utility model relates to a kind of electrolytic phosphating of steel wires treatment unit.
Background technology
China's current merchant wire industry ubiquity three large long history pollution problems.I.e. " lead bath furnace " pollution, " pickling ", " phosphatization ", the three large difficult problems of polluting, the known disclosed patent No. is ZL2008101046064, patent name " multifunctional steel wire induction heating heat-treatment device and method ", solve " lead bath furnace " pollution problem that steel wire industry has been continued to use more than 100 years, but also have two to pollute a difficult problem: pickling, phosphatization, still unresolved.Therefore, need to provide a kind of new technical scheme to solve the problems referred to above.
Utility model content
For addressing the above problem, the utility model provides a kind of electrolytic phosphating of steel wires treatment unit.This device has solved a pollution difficult problem for pickling, phosphatization.
The technical solution adopted in the utility model is:
Electrolytic phosphating of steel wires treatment unit, this phosphating treatment device comprises electrolytic solution treatment system, electrolytic phosphating treatment system, saponification conservation treatment system and the drying and processing system that the steel wire that makes after thermal treatment is inputted successively.
Described electrolytic solution treatment system comprises electrode, electrolytic solution groove, liquid-storing box and solution feed pump, described electrode and electrolytic solution groove are all fixed on resting support, described electrode is installed on electrolytic bath front end, and described electrolytic solution trench bottom is communicated with solution feed pump, and described solution feed pump is placed on liquid-storing box.
Described electrolytic solution groove top is connected with resting support top by resting support drag-line.
Described electrolytic phosphating treatment system comprises electrode I, Phosphating Slot, phosphatization liquid pump and Phosphating Solution case, described electrode I and Phosphating Slot are all fixed on resting support, described electrode I is installed on Phosphating Slot front end, and described Phosphating Slot bottom is communicated with phosphatization liquid pump, and described phosphatization liquid pump is placed on Phosphating Solution case.
Described Phosphating Slot both sides are connected with resting support top by resting support drag-line.
Described electrolytic solution groove and Phosphating Slot include the anodal current wiring terminal in shell, shell, anodal electrical current carriers and steel wire steady arm, described steel wire steady arm is installed in anodal electrical current carriers, described anodal electrical current carriers bottom connects anodal current wiring terminal one end, and the described anodal current wiring terminal the other end stretches out shell.
Described saponification conservation treatment system comprises that saponification liquid bath, saponification liquid pump and saponification liquor deposit tank, and described saponification liquid bath is fixed on resting support, and described saponification liquor trench bottom is communicated with saponification liquid pump, and described saponification liquid pump is placed in saponification liquor and deposits on tank.
Described drying and processing system comprises baker and baker electro-heat equipment, and described baker is installed on baker electro-heat equipment top.
The beneficial effects of the utility model: steel wire input electrolytic phosphating treatment unit after heat treatment; after electrolytic solution processing, electrolytic phosphating processing, saponification conservation treatment, drying and processing; a little remaining oxide compound of surface of steel wire is eliminated very soon under ionizing event; after processing by saponification; alramenting layer is adequately protected; again the saponification liquor of Steel Wire Surface is dried, reduced pollution problem.
Brief description of the drawings
Fig. 1 is device schematic diagram of the present utility model.
Fig. 2 is that the utility model is along A-A to sectional view.
Wherein: 1, electrode I, 2, resting support, 3, electrolytic solution groove, 4, liquid-storing box, 5, solution feed pump, 6, Phosphating Slot, 7, phosphatization liquid pump, 8, Phosphating Solution case, 9, saponification liquid bath, 10, saponification liquid pump, 11, saponification liquor is deposited tank, and 12, baker, 13, baker electro-heat equipment, 14, electrode II, 15, shell, 16, anodal current wiring terminal, 17, anodal electrical current carriers, 18, steel wire steady arm, 19, resting support drag-line.
Embodiment
In order to deepen understanding of the present utility model, below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, and this embodiment only, for explaining the utility model, does not form the restriction to protection domain of the present utility model.
As shown in Figure 1, electrolytic phosphating of steel wires treatment unit of the present utility model, this phosphating treatment device comprises electrolytic solution treatment system, electrolytic phosphating treatment system, saponification conservation treatment system and the drying and processing system that the steel wire that makes after thermal treatment is inputted successively.
Electrolytic solution treatment system comprises electrode I 1, electrolytic solution groove 3, liquid-storing box 4 and solution feed pump 5, electrode I 1 and electrolytic solution groove 3 are all fixed on resting support 2, electrode I 1 is installed on electrolytic solution groove 3 front ends, and electrolytic solution groove 3 bottoms are communicated with solution feed pump 5, and solution feed pump 5 is placed on liquid-storing box 4.Electrode I 1 output negative pole electric current, when in the liquid of the anodal electric charge of the steel wire input tape with cathode charge, under electrolytic solution groove 3 electrolytic action, the oxide compound fast-falling of Steel Wire Surface, substitute acid cleaning process process, liquid-storing box 4 is held into the liquid recycling, required circulation fluid in solution feed pump 5 electrolysis solution tanks 3.
Electrolytic solution groove 3 tops are connected with resting support 2 tops by resting support drag-line 19.Resting support drag-line 19 utilizes the rigidity of resting support 2 to hold cell body, guarantees the supporting capacity of cell body.
Electrolytic phosphating treatment system comprises electrode II 14, Phosphating Slot 6, phosphatization liquid pump 7 and Phosphating Solution case 8, electrode II 14 output negative pole electric currents, be arranged on Phosphating Slot 6 front ends, electrode II 14 and Phosphating Slot 6 are all fixed on resting support 2, electrode II 14 is installed on Phosphating Slot 6 front ends, Phosphating Slot 6 bottoms are communicated with phosphatization liquid pump 7, and phosphatization liquid pump 7 is placed on Phosphating Solution case 8.The steel wire of input from electrolytic solution groove 3 is entered to surface granosealing in Phosphating Slot 6, and phosphatization liquid pump 7 provides the Phosphating Solution recycling, and Phosphating Solution case 8 is deposited and held the Phosphating Solution recycling.
Phosphating Slot 6 both sides are connected with resting support 2 tops by resting support drag-line 19.Resting support drag-line 19 utilizes the rigidity of resting support 2 to hold cell body, guarantees the supporting capacity of cell body.
In Fig. 2, electrolytic solution groove 3 and Phosphating Slot 6 include anodal current wiring terminal 16, anodal electrical current carriers 17 and the steel wire steady arm 18 in shell 15, shell 15, steel wire steady arm 18 is installed in anodal electrical current carriers 17, anodal electrical current carriers 17 bottoms connect anodal current wiring terminal 16 one end, and anodal current wiring terminal 16 the other ends stretch out shell 15.Shell 15 is on-metallic article, as the container of electrolytic solution, make its electrolytic solution have the space of a circulation, anodal current wiring terminal 16 impels anodal electrical current carriers charged from the positive electrode current of rectifier power source input, anodal electrical current carriers 17 is metalwork, when after positive electrode current input, whole carrier is all charged, liquid in groove is thereupon charged like this, carrier lengths power is less than cell body length, steel wire steady arm 18 is controlled steel wire and in groove, is done the high-speed straight-line vibration in when motion, straight stable while ensureing steel wire translational motion.
Saponification conservation treatment system comprises that saponification liquid bath 9, saponification liquid pump 10 and saponification liquor deposit tank 11, and saponification liquid bath 9 is fixed on resting support 2, and saponification liquid bath 9 bottoms are communicated with saponification liquid pump 10, and saponification liquid pump 10 is placed in saponification liquor and deposits on tank 11.Saponification liquid bath 9 is made saponification conservation treatment the steel wire after alramenting, and saponification liquid pump 10 provides the saponification liquor recycling, and saponification liquor is deposited tank 11 and deposited the saponification liquor recycling.
Drying and processing system comprises baker 12 and baker electro-heat equipment 13, and baker 12 is installed on baker electro-heat equipment 13 tops.Baker 12 is dried steel wire, and baker electro-heat equipment 13 provides constant heat.
Working process and principle
When the steel wire horizontality translational motion by after induction heating water smoke isothermal processes is during through electrode I 1, steel wire body enters electrolytic solution groove 3 with constant cathode charge, liquid in electrolytic bath 3 is due to non-metal shell 15, the function of anodal current wiring terminal 16, make it with anodal electric charge, a little remaining oxide compound of the surface of steel wire is eliminated very soon under ionizing event like this, the negative charge of steel wire body is in a constant scope simultaneously, the rear steel wire body of input Phosphating Slot 6 negative charge is more stable, when steel wire continues translational motion to electrode II 14, again through constant cathodal current input, then enter Phosphating Slot 6, structure in Phosphating Slot 6 is identical with the structure in electrolytic solution groove 3, by the parts identical with anodal current wiring terminal, input positive electrode current, impel the anodal electric charge of Phosphating Solution band, steel wire body is electronegative like this, Phosphating Solution positively charged, in this state, by (steel wire movement velocity and the steel wire time in electrolytic phosphating liquid is a kind of funtcional relationship) after certain distance, steel wire body surface has produced good phosphate coating, then steel wire input saponification liquid bath 9, in saponification liquid bath 9, be not with any auxiliary spare part, fill with saponification liquor, after processing by saponification, alramenting layer is adequately protected, input again baker 12, temperature in baker 12 is the heat energy that baker electro-heat equipment 13 provides, major function is that the saponification liquor of Steel Wire Surface is dried, allow steel wire enter final take-up operation stage.
Liquid-storing box 4 in device, solution feed pump 5 are circulation members of solution, solution is inputted in electrolytic solution groove 3 through solution feed pump 5, reflux is arranged at electrolytic solution groove 3 bottoms, through flowing of solution in groove, the oxide compound of a little deposition is taken back in liquid-storing box 4, in liquid-storing box 4, had filtration facility, the solution after filtration is inputted electrolytic solution groove 3 through solution feed pump 5 again, form such recurrent state of going round and beginning again, in solution, be not with any medium.
The working process of phosphatization liquid pump 7 and Phosphating Solution storage box 8 is identical with electrolytic solution groove 3 systems.Phosphating Solution is in recycling, and effective constituent can be successively decreased, according to the rational interpolation that likens to of the initial total mass in the steel wire total mass of having processed and liquid-storing box.Phosphating Solution does not need to change and discharge, and this is to solve the novelty science and technology measure that produces pollution problem in original parkerizing process.
It is steel wires that saponification securing system is inputted from Phosphating Slot 6 that saponification liquid bath 9, saponification liquid pump 10, saponification liquor are deposited tank 11, and the existing phosphate coating in surface covers, and through transition in the saponification liquor of certain distance certain temperature, the phosphate coating on surface is effectively protected.
The drying and processing system that baker 12 and baker electro-heat equipment 13 form, it dries the Steel Wire Surface of input.The temperature of baking needed suitably regulates according to the point-to-point speed of steel wire.
Resting support 2, steel wire steady arm 18 are supporting and fixed sturctures of overall structure, and resting support 2 is mainly to fix with ground and as certain supporting-point.Because groove body is non-metallic material, when work, in groove, there is a large amount of liquid, groove body is longer, and the below of groove body has many auxiliaries to lay, and therefore degree of collapsing is large, solves the bearing capacity of cell body by the effect of steel wire steady arm 18.
Rectified current is arranged on resting support 2 by the actual needs of operating mode, the electric current of general supply input is made after rectification processing to connection electrode I 1, electrode II 14, anodal current wiring terminal 16.Electrode I 1,14 of electrode II need to install 2, anodal current wiring terminal 16 is according to different handling objects (wire diameter of steel wire, material), in anodal electrical current carriers 17, choose suitable packing density and spacing distance, guarantee the reliable, perfect of electrolysis process, reach design objective.
Claims (8)
1. electrolytic phosphating of steel wires treatment unit, is characterized in that: this phosphating treatment device comprises electrolytic solution treatment system, electrolytic phosphating treatment system, saponification conservation treatment system and the drying and processing system that the steel wire that makes after thermal treatment is inputted successively.
2. electrolytic phosphating of steel wires treatment unit according to claim 1, it is characterized in that: described electrolytic solution treatment system comprises electrode I, electrolytic solution groove, liquid-storing box and solution feed pump, described electrode I and electrolytic solution groove are all fixed on resting support, described electrode I is installed on electrolytic solution front of the slot, described electrolytic solution trench bottom is communicated with solution feed pump, and described solution feed pump is placed on liquid-storing box.
3. electrolytic phosphating of steel wires treatment unit according to claim 2, is characterized in that: described electrolytic solution groove top is connected with resting support top by resting support drag-line.
4. electrolytic phosphating of steel wires treatment unit according to claim 1, it is characterized in that: described electrolytic phosphating treatment system comprises electrode II, Phosphating Slot, phosphatization liquid pump and Phosphating Solution case, described electrode II and Phosphating Slot are all fixed on resting support, described electrode II is installed on Phosphating Slot front end, described Phosphating Slot bottom is communicated with phosphatization liquid pump, and described phosphatization liquid pump is placed on Phosphating Solution case.
5. electrolytic phosphating of steel wires treatment unit according to claim 4, is characterized in that: described Phosphating Slot both sides are connected with resting support top by resting support drag-line.
6. according to the electrolytic phosphating of steel wires treatment unit described in claim 2 or 4, it is characterized in that: described electrolytic solution groove and Phosphating Slot include the anodal current wiring terminal in shell, shell, anodal electrical current carriers and steel wire steady arm, described steel wire steady arm is installed in anodal electrical current carriers, described anodal electrical current carriers bottom connects anodal current wiring terminal one end, and the described anodal current wiring terminal the other end stretches out shell.
7. electrolytic phosphating of steel wires treatment unit according to claim 1; it is characterized in that: described saponification conservation treatment system comprises that saponification liquid bath, saponification liquid pump and saponification liquor deposit tank; described saponification liquid bath is fixed on resting support; described saponification liquor trench bottom is communicated with saponification liquid pump, and described saponification liquid pump is placed in saponification liquor and deposits on tank.
8. electrolytic phosphating of steel wires treatment unit according to claim 1, is characterized in that: described drying and processing system comprises baker and baker electro-heat equipment, and described baker is installed on baker electro-heat equipment top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320851510.0U CN203754838U (en) | 2013-12-23 | 2013-12-23 | Steel wire electrolysis phosphating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320851510.0U CN203754838U (en) | 2013-12-23 | 2013-12-23 | Steel wire electrolysis phosphating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203754838U true CN203754838U (en) | 2014-08-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320851510.0U Expired - Fee Related CN203754838U (en) | 2013-12-23 | 2013-12-23 | Steel wire electrolysis phosphating device |
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| Country | Link |
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| CN (1) | CN203754838U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103741195A (en) * | 2013-12-23 | 2014-04-23 | 南通恒新金属工艺科技有限公司 | Steel wire electrolysis and parkerizing device |
-
2013
- 2013-12-23 CN CN201320851510.0U patent/CN203754838U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103741195A (en) * | 2013-12-23 | 2014-04-23 | 南通恒新金属工艺科技有限公司 | Steel wire electrolysis and parkerizing device |
| CN103741195B (en) * | 2013-12-23 | 2016-06-15 | 南通恒新金属工艺科技有限公司 | Electrolytic phosphating of steel wires processes device |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 Termination date: 20171223 |