CN208685103U - A kind of electrolysis method scale removal equipment - Google Patents

A kind of electrolysis method scale removal equipment Download PDF

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Publication number
CN208685103U
CN208685103U CN201820964262.3U CN201820964262U CN208685103U CN 208685103 U CN208685103 U CN 208685103U CN 201820964262 U CN201820964262 U CN 201820964262U CN 208685103 U CN208685103 U CN 208685103U
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electrode
electrolysis
stretch bending
cathode
electrolytic
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CN201820964262.3U
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Chinese (zh)
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夏征
王爽
陈国利
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Abstract

The utility model provides a kind of electrolysis method scale removal equipment, including uncoiler, stretch bending descaling mill, drive tensioner, winder, the uncoiler is used to for coiled sheet metal being unfolded, and it is transported to stretch bending descaling mill, the side of the uncoiler is equipped with stretch bending descaling mill, the stretch bending descaling mill is for thicker oxide skin to be crushed during stretch bending, the side of the stretch bending descaling mill is equipped with several drive tensioners, the side of the drive tensioner is equipped with winder, it is characterized by also including electrolysis installations, electrolysis installation is equipped between two drive tensioners between the drive tensioner and winder.The utility model has the beneficial effects that economic, efficient, environmental protection, completely substitution chemical pickling descale.

Description

A kind of electrolysis method scale removal equipment
Technical field
The utility model belongs to metal removal oxide skin apparatus field, sets more particularly, to a kind of electrolysis method scale removal It is standby.
Background technique
Hot-rolled steel because carrying out at high temperature, and the unavoidable steel that will cause is chemically reacted with the oxygen in air, on surface It will form certain thickness oxide skin, the general three-decker composition of the oxide skin after finish to gauge, steel matrix is respectively oxygen from inside to outside Change ferrous iron and account for about the 40%~95% of oxide skin overall thickness, is loose, porous fine crystallization tissue;Middle layer is ferroso-ferric oxide Account for about the 4%~14% of overall thickness, is fine and close, non-porous and crack glass break magnetic tissue;Outermost layer is three oxidations two Iron accounts for about the 1%~2% of overall thickness, is the iron oxide of crystal structure;Oxide skin overall thickness is generally 6.5um~15um.Due to The generation of oxide skin and developmental process are influenced by conditions such as temperature and times, so steel band is naturally cold in finish to gauge and after batching But ferrous oxide can gradually change to ferroso-ferric oxide during, the final accounting for changing oxide skin three-decker.From the above oxygen Change skin generating process to see, essence is exactly the oxidation process of iron;From the removal of oxide skin in terms of property angle, ferrous oxide is easy Removal, the high oxide ferroso-ferric oxide of mainly iron is to be difficult to remove, and people have taken a variety of methods and handled The oxide skin generated in the production process.
The processing most common method of oxide skin is oxygen caused by acid wash is removed such as the method for still pickling because of hot rolling at present Compound produces a large amount of spent acid discharge in the process, extremely serious pollution is caused to environment, right in operation Staff and its equipment damage.
In addition to traditional acid washing method, there are also traditional electrolyte method, water sand-blast, traditional brushing methods (Mechanical Method) etc..It is other It is some for example, laser, plasma etc. are even more the method for earth-free gas, although can remove or higher cost or be exactly to imitate Rate is extremely low, very impracticable;Traditional electrolyte method, water sand-blast, in traditional steel wire brushing method (Mechanical Method) each all or mostly or Few there are some problems, so that metallurgy industry, up to the present handles oxide skin, or extremely dirty using causing to environment Dye and the extremely severe acid washing method of working environment.
Traditional electrolyte method, such as CN1266650A, because export license, flow of electrolyte are big, more projection electrode spacing is excessive, So that power consumption is very big, electric utilization rate is very low, most is heated to electrolyte again, cannot solve at all in industry at present Certainly, cause this method unpractical feasibility at all.If shortening interelectrode distance, it will cause short circuits, can not carry out electricity Solution.
In particular, it should be pointed out that traditional brushing method, since traditional brushing method is in the presence of the oxidation that can not be removed in tiny pit The problems such as object and low production efficiency, is difficult to realize industrialized mass production, and bristle is that line contacts mill with steel part processed It cuts, the quality for the treatment of effect, mainly there is the number of brush roll quantity to determine, the increase of brush roll quantity is directly related to transfer motion power Size, and then influence processing cost and efficiency;The method can not preferably solve always bristle at work with the mill of steel part After damage, backlash compensation problem between bristle and steel part causes this method to fail to obtain popularization and application;In addition many traditional brushes Mill method is if it is intended to handle the oxide in tiny pit, the method for use is then hard grind of going into overdrive, so that causing convex Useful steel is also worn at rising, while the probability that brush roll is worn greatly improves, to cause to be lost excessive.
Utility model content
The purpose of this utility model is to solve the problems, such as pickling must be used to provide in the method for traditional scale removal A kind of economical, efficient, environmental protection scale removal equipment and minimizing technology, the oxidation being especially suitable on removal steel class plate Object.
The technical solution of the utility model is: a kind of electrolysis method scale removal equipment, including uncoiler, stretch bending scale breading Machine, drive tensioner, winder, the uncoiler is used to for coiled sheet metal being unfolded, and is transported to stretch bending descaling mill, The side of the uncoiler is equipped with stretch bending descaling mill, and the stretch bending descaling mill is used for thicker oxide skin during stretch bending It is crushed, the side of the stretch bending descaling mill is equipped with several drive tensioners, and the drive tensioner includes first The horizontal side of power roller, the second jockey pulley, power motor, first jockey pulley is equipped with the second jockey pulley, first tension Roller and the second jockey pulley are driven by power motor, and it further includes electrolysis installation that the side of the drive tensioner, which is equipped with winder, Electrolysis installation is equipped between the drive tensioner and winder;
Further, the electrolysis installation includes washing room, tank house, and the electrolysis installation is interior along the sheet metal side of entrance It is successively arranged washing room, tank house to exit axis, is equipped with several electrolytic modules, several described electrolysis in the tank house Module forms electrolysis assembly line, to the oxide skin being electrolysed after free abrasive material constraint is ground in sheet metal surface pit, institute The other side for stating electrolysis assembly line is equipped with several brush rolls, to scrub by being attached to the anti-of sheet metal surface after electrolytic module Product is answered, the bottom in the electrolysis installation is wastewater collection pond, the Sewage treatment pond and external Sewage treatment filtering ponds It is connected, recycles filtered water and be transmitted back in washing room by water pump;
Further, the electrolytic module includes anode electrolytic tank and cathode electrolytic cell, the anode electrolytic tank and cathode The both ends of electrolytic cell are equipped with opening, into and out to sheet metal, set in the anode electrolytic tank and cathode electrolytic cell There is electrolyte, the anode electrolytic tank and the cathode electrolytic cell are horizontally spaced about, and the anode electrolytic tank includes Anodic Electrode, lower anode electrode, the Anodic electrode and lower anode electrode setting symmetrical above and below, intermediate there are total sheet metals to pass through And the gap of electrolysis is completed, the cathode electrolytic cell includes upper cathode electrode, lower cathode electrode, the upper cathode electrode and lower yin The setting symmetrical above and below of pole electrode, centre pass through there are total sheet metal and complete the gap of electrolysis, and the upper cathode electrode is under Cathode electrode setting symmetrical above and below, centre pass through there are total sheet metal and completes be electrolysed gap, the Anodic electrode, under The side of anode electrode and upper cathode electrode, lower cathode electrode is equipped with electrolysis nozzle for liquid;
Further, the Anodic electrode and upper cathode electrode are that lower section is equipped with the plate type electrode with insulation bristle, institute It states lower anode electrode and lower cathode electrode is that top is equipped with the plate type electrode with insulation bristle;
Further, the Anodic electrode, lower anode electrode, upper cathode electrode, lower cathode electrode are to be surrounded by insulation The welding roll of permeable wear-resistant material;
A kind of minimizing technology of electrolysis method scale removal equipment: including physics scale breading, electrolysis step:
Physics scale breading: sheet metal is transported on stretch bending descaling mill after being unfolded by uncoiler, and it is broken to carry out physics;
Electrolysis: sheet metal is completed to enter in electrolysis installation after drive tensioner after physics is broken, is being electrolysed In module, if it is plate type electrode, since Anodic electrode and upper cathode electrode are that lower section is equipped with the board-like electricity with insulation bristle Pole, lower anode electrode and lower cathode electrode are that top also is provided with the plate type electrode with insulation bristle, and sheet metal moves through Cell reaction occurs for anode electrode, lower anode electrode or upper cathode electrode, lower cathode electrode surface simultaneously, and the bristle that insulate is to metal The constantly flexible scrub in plate front and back sides, constantly product after removal reaction, make to continuously leak out to reaction surface, anti-to accelerate electrolysis It answers, while between sheet metal and Anodic electrode and lower anode electrode or sheet metal and upper cathode electrode and lower cathode electrode Gap be not empty, but replaced by insulation bristle, both insulated, also reduce Anodic electrode and lower anode electrode, The distance between upper cathode electrode and lower cathode electrode, sheet metal enter next drive tension after electrolysis installation Winder is entered back into after roller carries out clot storage.
The utility model has the advantages and positive effects of: due to the adoption of the above technical scheme, real in electrolytic process It is smaller electrode spacing is showed, power consumption is smaller, and electric utilization rate is higher;Give up husky and waste water during polishing and electrolysis It is recycled, realizes environmentally protective.
Detailed description of the invention
Fig. 1 is the overall mechanism schematic diagram of the utility model;
Fig. 2 is the structural schematic diagram of the electrolytic module of the utility model;
Fig. 3 is the electrolysis principle figure of the utility model.
In figure:
Uncoiler 1, stretch bending descaling mill 2, drive tensioner 3, the first jockey pulley 31, the second jockey pulley 32, winder 4, Sheet metal 5, electrolysis installation 6, washing room 61, tank house 62, electrolytic module 621, anode electrolytic tank 621a, Anodic electrode 621aa, lower anode electrode 621ab, cathode electrolytic cell 621b, upper cathode electrode 621ba, lower cathode electrode 621bb, electrolyte spray Mouth 621c, insulation bristle 621d, electrolyte 621e, brush roll 622, wastewater collection pond 63, Sewage treatment filtering ponds 64, water pump 65.
Specific embodiment
It elaborates with reference to the accompanying drawing to the utility model.
As shown in Figure 1, 2, a kind of electrolysis method scale removal equipment of the utility model, including uncoiler 1, stretch bending descaling mill 2, drive tensioner 3, winder 4, the uncoiler 1 are transported to stretch bending scale breading for coiled sheet metal 5 to be unfolded Machine 2, the side of the uncoiler 1 are equipped with stretch bending descaling mill 2, and the stretch bending descaling mill 2 is used for thicker oxide skin in stretch bending During be crushed, the side of the stretch bending descaling mill 2 is equipped with several drive tensioners 3, the drive tensioner 3 Including the first jockey pulley 31, the second jockey pulley 32, power motor (not shown), the horizontal side of first jockey pulley 31 is equipped with Second jockey pulley 31, first jockey pulley 31 and the second jockey pulley 32 are driven by power motor, the drive tensioner 3 Side is equipped with winder 4, further includes electrolysis installation 6, and electrolysis installation is equipped between the drive tensioner 3 and winder 4 6;
Further, the electrolysis installation 6 includes washing room 61, tank house 62, and the electrolysis installation 6 is interior along sheet metal 5 approach axis are successively arranged washing room 61, tank house 62 to exit axis, are equipped with several electrolytic modules 621 in the tank house, Several described electrolytic modules 621 form electrolysis assembly line, to be electrolysed 5 surface of sheet metal after free abrasive material constraint is ground The other side of oxide skin in pit, the electrolysis assembly line is equipped with several brush rolls 622, to scrub through electrolytic module 621 It is attached to the reaction product on 5 surface of sheet metal afterwards, the bottom in the electrolysis installation 6 is wastewater collection pond 63, the waste water Recovery pond 63 is connected with external Sewage treatment filtering ponds 64, recycles filtered water by water pump 65 and is transmitted back to washing room 61 It is interior;
Further, institute's electrolytic module 621 includes anode electrolytic tank 621a and cathode electrolytic cell 621b, the anode The both ends of electrolytic cell 621a and cathode electrolytic cell 621b are equipped with opening, into and out to sheet metal 5, the anode electricity It solves and is equipped with electrolyte 621e, the anode electrolytic tank 621a and the cathode electrolytic cell in slot 621a and cathode electrolytic cell 621b 621b is horizontally spaced about, and the anode electrolytic tank 621a includes Anodic electrode 621aa, lower anode electrode 621ab, it is described on Anode electrode 621aa and lower anode electrode 621ab setting symmetrical above and below, centre pass through there are total sheet metal 5 and complete electrolysis Gap, the cathode electrolytic cell 621b includes upper cathode electrode 621ba, lower cathode electrode 621bb, the upper cathode electrode 621ba and lower cathode electrode 621bb setting symmetrical above and below, centre pass through there are total sheet metal 5 and complete the gap of electrolysis, institute Cathode electrode 621ba and lower cathode electrode 621bb setting symmetrical above and below are stated, centre passes through and completes there are total sheet metal 5 The gap of electrolysis, the Anodic electrode 621aa, lower anode electrode 621ab and upper cathode electrode 621ba, lower cathode electrode The side of 621bb is equipped with electrolysis nozzle for liquid 621c;
Further, the Anodic electrode 621aa and upper cathode electrode 621ab is that lower section is equipped with band insulation bristle 621d Plate type electrode, the lower anode electrode 621ab and lower cathode electrode 621aa are that top is equipped with band and insulate the board-like of bristle 621d Electrode;
Further, the Anodic electrode 621aa, lower anode electrode 621ab, upper cathode electrode 621ba, lower cathode electricity Pole 621bb is the welding roll for being surrounded by the permeable wear-resistant material that insulate;
A kind of minimizing technology of combined type scale removal equipment: including physics scale breading, constraint grinding, electrolysis step:
Physics scale breading: sheet metal 5 is transported on stretch bending descaling mill after being unfolded by uncoiler, is carried out physics and is crushed, will be big Block oxide skin is crushed, and falls removal during winding and advancing after broken;
Electrolysis: sheet metal 5 is completed to enter after drive tensioner 3 in electrolysis installation 6 after physics is broken, in electricity It solves in module 621, if it is plate type electrode, since Anodic electrode 621aa and upper cathode electrode 621ba is that lower section is equipped with band absolutely The plate type electrode of edge bristle 621d, lower anode electrode 621ab and lower cathode electrode 621bb are that top also is provided with band insulation bristle The plate type electrode of 621d, sheet metal 5 move through Anodic electrode 621aa, lower anode electrode 621ab or upper cathode electrode Cell reaction occurs for 621ba, the surface lower cathode electrode 621bb simultaneously, and insulation bristle 621d is constantly soft to 5 front and back sides of sheet metal Property scrub, constantly product after removal reaction, make to continuously leak out to reaction surface, to accelerate cell reaction, while sheet metal 5 with Anodic electrode 621aa and lower anode electrode 621ab or sheet metal 5 and upper cathode electrode 621ba and lower cathode electrode 621bb Between gap be not empty, but replaced by insulation bristle 621d, both insulated, and also reduced Anodic electrode 621aa With the distance between lower anode electrode 621ab, upper cathode electrode 621ba and lower cathode electrode 621bb, to reduce energy consumption; If it is the welding roll for being surrounded by the permeable wear-resistant material that insulate, principle is to reduce electrode by being surrounded by the permeable wear-resistant material of insulation The distance between, while it can also insulate, to reduce energy consumption, because of depositing for insulation bristle 621d or the permeable wear-resistant material that insulate And apart from can be in order to avoid contact of the sheet metal with electrode, causes short circuit in the smallest situation;In anode electrolytic tank 621a Sheet metal 5 is that cathode restores to obtain electron reaction, high price oxygen with respect to Anodic electrode 621aa and lower anode electrode 621ab Compound is reduced to metal simple-substance, the relatively upper cathode electrode 621ba of sheet metal and lower cathode electrode in cathode electrolytic cell 621b 621bb is that oxidation betatopic reaction occurs for anode, and metal simple-substance loses electronics and is dissolved in electrolyte in the form of an ion, then in electricity Hydroxide ion in solution liquid forms compound and precipitates and filter out in the electrolytic solution;Direction of current flow are as follows: positive pole → conducting wire → Anodic electrode and lower anode electrode → anode electrolytic tank electrolysis liquid → sheet metal → cathode electrolytic cell electrolyte → upper cathode electrode and lower cathode electrode → conducting wire → power cathode;
Sheet metal enters next washing room after electrolysis installation, is rinsed again, enters finally into winding Machine carries out clot storage.
One embodiment of the utility model is described in detail above, but the content is only the utility model Preferred embodiment should not be considered as limiting the scope of the present invention.It is all to be made according to application scope of the utility model All the changes and improvements etc., should still belong within the patent covering scope of the utility model.

Claims (5)

1. a kind of electrolysis method scale removal equipment, including uncoiler, stretch bending descaling mill, drive tensioner, winder, described Uncoiler is used to for coiled sheet metal being unfolded, and is transported to stretch bending descaling mill, and the side of the uncoiler is broken equipped with stretch bending Squama machine, the stretch bending descaling mill are used to for thicker oxide skin being crushed during stretch bending, the stretch bending descaling mill Side is equipped with several drive tensioners, and the drive tensioner includes the first jockey pulley, the second jockey pulley, power motor, The horizontal side of first jockey pulley is equipped with the second jockey pulley, and first jockey pulley and the second jockey pulley are passed by power motor Dynamic, the side of the drive tensioner is equipped with winder, it is characterised in that: further includes electrolysis installation, in the drive Electrolysis installation is equipped between power machine and winder.
2. a kind of electrolysis method scale removal equipment according to claim 1, it is characterised in that: the electrolysis installation includes Washing room, tank house, the electrolysis installation is interior to be successively arranged washing room, electrolysis along sheet metal approach axis to exit axis Room, the tank house is interior to be equipped with several electrolytic modules, several described electrolytic modules form electrolysis assembly lines, free to be electrolysed Abrasive material constraint grinding after oxide skin in sheet metal surface pit, the other side of the electrolysis assembly line is equipped with several brushes Roller, to scrub the reaction product by being attached to sheet metal surface after electrolytic module, the bottom in the electrolysis installation is Wastewater collection pond, the Sewage treatment pond are connected with external Sewage treatment filtering ponds, and it is defeated by water pump to recycle filtered water It sends back in washing room.
3. a kind of electrolysis method scale removal equipment according to claim 2, it is characterised in that: the electrolytic module includes The both ends of anode electrolytic tank and cathode electrolytic cell, the anode electrolytic tank and cathode electrolytic cell are equipped with opening, to metal plate Material is into and out, and electrolyte, the anode electrolytic tank and the cathode are equipped in the anode electrolytic tank and cathode electrolytic cell Electrolytic cell is horizontally spaced about, and the anode electrolytic tank includes Anodic electrode, lower anode electrode, and the Anodic electrode is under Anode electrode setting symmetrical above and below, centre pass through there are total sheet metal and complete the gap of electrolysis, the cathode electrolytic cell packet Include cathode electrode, lower cathode electrode, the one of the Anodic electrode, lower anode electrode and upper cathode electrode, lower cathode electrode Side is equipped with electrolysis nozzle for liquid.
4. a kind of electrolysis method scale removal equipment according to claim 3, it is characterised in that: the Anodic electrode and Upper cathode electrode is that lower section is equipped with the plate type electrode with insulation bristle, and the lower anode electrode and lower cathode electrode are equipped with for top Plate type electrode with insulation bristle.
5. a kind of electrolysis method scale removal equipment according to claim 3, it is characterised in that: the Anodic electrode, Lower anode electrode, upper cathode electrode, lower cathode electrode are the welding roll for being surrounded by the permeable wear-resistant material that insulate.
CN201820964262.3U 2018-06-19 2018-06-19 A kind of electrolysis method scale removal equipment Expired - Fee Related CN208685103U (en)

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Application Number Priority Date Filing Date Title
CN201820964262.3U CN208685103U (en) 2018-06-19 2018-06-19 A kind of electrolysis method scale removal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820964262.3U CN208685103U (en) 2018-06-19 2018-06-19 A kind of electrolysis method scale removal equipment

Publications (1)

Publication Number Publication Date
CN208685103U true CN208685103U (en) 2019-04-02

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Application Number Title Priority Date Filing Date
CN201820964262.3U Expired - Fee Related CN208685103U (en) 2018-06-19 2018-06-19 A kind of electrolysis method scale removal equipment

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Granted publication date: 20190402

Termination date: 20200619