CN2095720U - Continuous pretreatment device for wire material surface - Google Patents

Continuous pretreatment device for wire material surface Download PDF

Info

Publication number
CN2095720U
CN2095720U CN 90214663 CN90214663U CN2095720U CN 2095720 U CN2095720 U CN 2095720U CN 90214663 CN90214663 CN 90214663 CN 90214663 U CN90214663 U CN 90214663U CN 2095720 U CN2095720 U CN 2095720U
Authority
CN
China
Prior art keywords
pickling
cell body
phosphor removal
metal wire
utility
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.)
Withdrawn
Application number
CN 90214663
Other languages
Chinese (zh)
Inventor
郑汉清
严一民
梁乐天
李一心
曹建清
赵茹梅
张澄埃
张士坤
陈正安
陆雪华
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.)
JIANYIN STEEL ROPE GENERAL FACTORY JIANGSU PROV
Original Assignee
JIANYIN STEEL ROPE GENERAL FACTORY JIANGSU PROV
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 JIANYIN STEEL ROPE GENERAL FACTORY JIANGSU PROV filed Critical JIANYIN STEEL ROPE GENERAL FACTORY JIANGSU PROV
Priority to CN 90214663 priority Critical patent/CN2095720U/en
Publication of CN2095720U publication Critical patent/CN2095720U/en
Withdrawn legal-status Critical Current

Links

Images

Abstract

The utility model relates to a continuous pretreatment device for wire material surfaces, which is used for continuous phosphor removal and coating of the surface of metal wire material, and the utility model belongs to the field of metallurgy. The existing surface phosphor removal adopts chemical phosphor removal or mechanical phosphor removal; the production cost is high, the environmental pollution is serious, and the phosphor removal quality is hard to control. The utility model is characterized in that a mechanical phosphor removal device, a flushing device, an electrolysis acid flushing device, a washing groove, a coating groove and a drawbench are arranged on the back of a paying out machine, and the pretreatment processes of phosphor removal, coating, wire drawing, etc. are combined into a continuous integral production device. The utility model has the advantages of high automatization, low cost, clean surface phosphor removal, basic no environmental pollution, less equipment investment and small occupation area.

Description

Continuous pretreatment device for wire material surface
The continuous pretreatment unit of a kind of wire surface is used for the continuous de-scaling of metal wire material surface, belongs to field of metallurgy.
At present, domestic chemical method and Mechanical Method are generally adopted in the metal wire material surface de-scaling.The chemical method of common use is that the whole wire rod of tying is immersed in de-scaling in the dilute sulfuric acid, and the Mechanical Method dephosphorization is removed surperficial firecoat with roll-type machinery with metal wire rod alternating bending distortion.
The deficiencies in the prior art part is: the investment of chemical method de-scaling main frame and corollary equipment is big, operating environment is poor, spent acid and exhausted air quantity is big, the control of de-scaling difficult quality, easily produce overpickling or handle unclean.Reasons such as Mechanical Method de-scaling metal material surface is coarse, electrostatic interaction and chemistry adhesion, the remaining squama amount in surface is bigger, is generally 0.84~1.22/kg.
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art part and provides a kind of wire surface continuous pretreatment unit, it is characterized in that: descaling bath is by hopper 4, bracket 5 and cathodic pickling cell body 6 are formed, cathodic pickling cell body 6 is by end face shrouding 7, pole plate 8, feed tube 9, leakage pipe 10 and pickling pipe 11 are formed, pickling pipe 11 top end openings, each cathodic pickling cell body 6 of cathodic pickling groove is with a polarity, pole plate 8 adopts opposed polarity, can be male or female, this device can be clean with the metal wire material surface de-scaling, improve work situation, investment and floor space are little.
Purpose of the present invention can reach by following measure: the metal wire rod after original mechanical descaling is become continuous pretreatment unit through flushed channel, cathodic pickling groove, rinse bath with painted groove, metal wire rod is come out → mechanical descaling → flushing → cathodic pickling → clean → be coated with lubricant → drawing → unwrapping wire by pay off rack.
Fig. 1 is roller arrangements figure, and the roller 2 of mechanical descaling device is 10~20, roller footpath D50~100MM, and roll spacing t60~80MM, roller are divided into 2~4 groups, and each organizes roller axis space interlaced arrangement each other.Because admission machine parts power a little for one of metal wire rod, with several groups of bending rolls metal wire rod is carried out alternating bending, and the wire rod surface fibre is enough extended, and reaches the de-scaling purpose, and metal wire rod is also had the aligning effect.Each organizes roller axis space interlaced arrangement each other, because metal wire rod by the different roller in locus, has not only been removed the firecoat of metal wire material surface, also the strain that produces after the roller alternating bending can be superposeed mutually, finally make full section obtain uniform plastic elongation, make the wire rod aligning.
D is relevant with diameter, the strength degree of metal wire rod in the roller footpath, if diameter is certain, the high more then roller of strength degree footpath is more little, and because of wire rod is hard more, distortion is just difficult more, make its surface fiber obtain stretching and must add larger radius of curvature, is generally 50~100mm.T is more little in roll spacing, and metal wire rod flexural deformation is big more, and scale removal effect is good more, but working roll is stressed big more, is generally 60~80mm.The roller number helps improving the de-scaling quality more, but can increase the sclerosis of metal wire rod and the traction power of take-up, and selection principle is under the prerequisite that guarantees the de-scaling quality, and the roller number is few as far as possible, is generally 10~20.
Fig. 2 is the flusher structural representation, and flushing can make the loose firecoat of remained on surface and dust remove to metal wire rod 1 through water, to improve the quality of next procedure.One nozzle 3 is arranged at the cell body bottom, and angle α is 30~50 ° between metal wire rod and nozzle, makes metal wire rod force flushing in adverse current, improves rinsing quality.
Fig. 3 is a cathodic pickling groove structural representation, is made up of hopper 4, bracket 5 and cathodic pickling cell body 6, and hopper 4 usefulness sheet metals are welded the inner bushing ring epoxy resins.Bracket 5 is made with epoxy resin by the channel-section steel lining, plays the effect of supporting cathodic pickling cell body 6.Fig. 4 is cathodic pickling trough body structure figure, Fig. 5 is a cathodic pickling cell body A-A profile, cathodic pickling cell body 6 is made up of end face shrouding 7, pole plate 8, feed tube 9, leakage pipe 10 and pickling pipe 11, metal wire rod 1 is by cathodic pickling cell body center, non-contact electrode, cathodic pickling cell body 6 has two compositions at least, and each pickling cell body 6 has only a polarity.Pickling pipe 11 materials are hard polvinyl choride pipe, and top end opening can be convenient to connect metal wire rod 1, and pole plate 8 general employings are being hanged down not diffluent metal material under the sour low-voltage, and commonly used is Plante-type plate inexpensive, easy purchase.In order to improve pickling speed and pickling quality, adopt the positive and negative utmost point to replace cathodic pickling, when the metal wire rod walking is in the descaling bath of anode the time at pole plate, metal wire rod is a negative electrode, because the electrode reflection, the hydrogen that metal wire rod is separated out plays reduction and mechanical stripping effect to its surperficial oxide; Otherwise when pole plate was negative electrode, metal wire rod was an anode, and the removal of surperficial firecoat is by means of the electrochemistry of metal and chemolysis, and the bubble that wire surface is separated out carries out the mechanical stripping firecoat.In the cathodic pickling process, pole plate alternately for the positive and negative utmost point, can be avoided " hydrogen embrittlement ", can not produce overpickling again.Cathodic pickling cell body 6 in the cathodic pickling groove has two compositions at least, and a pole plate is an anode, and one be negative electrode, and each cathodic pickling cell body 6 has only a polarity, crossfire not mutually between the interior electrolytic solution of cell body.Fig. 6 is a cathodic pickling slot number schematic diagram, polarity of each pickling cell body band in the cathodic pickling groove, pole plate 8 adopts different polarity, but the polarity positive and negative utmost point that is pole plate replaces, negative electrode of also several anodes, decide by cathodic pickling requirement quality, the anodic acid pickling cell body is more than the negative electrode cell body, and the cathodic pickling quality is good.
Sulfuric acid concentration is 150~200g/ liter, excessive overpickling and the hydrogen embrittlement of easily causing of concentration, and concentration is too small, and pickling is insufficient.The pickling time is generally about 10~15 seconds, for guaranteeing cathodic pickling quality, the Fe in the pickle + 2Concentration should be controlled at below the 250g/ liter, and pickling temperature is less than 60 ℃.
Metal wire rod after the cathodic pickling is through water washing device, and rinse water is a hot water, and its effect is residual acid solution and the foreign material that can remove on the metal wire rod, and metal wire rod is preheating to 70~80 ℃, for road coating operation is ready down.
Fig. 7 is the painted groove structure chart, and painted groove is made up of liquid suction pipe 12, silk rolling mould 13, silk rolling groove 14, feed tube 15, liquid storage tank 16, metal wire rod 1 surface is coated with lubricant is for the drawing speed that improves metal wire rod, reduces pulling capacity.
General coating is a borax, is example to be coated with boron, is coated with general 2~4 seconds of boron time, and solution temperature is controlled at about 70 ℃, and borax soln concentration is 250~350 grams per liters, and its pH value is between 9.0~9.4.
So far, metal wire material surface mechanical descaling, chemical de-scaling and coating are all finished, according to the processing needs wire drawing machine can be set, and the metal wire rod of coating lubricant is entered drawing-die carry out the prestretching preliminary working, then by the admission machine take-up; Can certainly be without wire drawing die, the metal wire rod that surface preparation is good is directly by the admission machine take-up.
If the good metal wire rod of preliminary treatment is without wire drawing die, the retractable linear velocity is then basic identical; Then according to its draft retractable linear velocity that converts, general take-up speed is 80~100 meters/minute through the metal wire rod of wire drawing die.
Characteristics of the present utility model are: with metal wire material surface mechanical descaling, cathodic pickling de-scaling, be coated with preprocessing process such as lubricant, wire drawing and be combined into continuous integrated production equipment.
Fig. 1 roller arrangements figure
Fig. 2 flusher structural representation
Fig. 3 cathodic pickling groove structural representation
Fig. 4 cathodic pickling trough body structure figure
Fig. 5 cathodic pickling cell body A-A profile
Fig. 6 cathodic pickling cell body polarity schematic diagram
Fig. 7 painted groove structure chart
Below in conjunction with embodiment the utility model is further set forth: the general diameter of high-speed rod is 5.5~6.5mm, and the steel wire that with the diameter is 6.0mm is an example, and the intensity of steel wire limit is 1500N/mm 2,, two bundle steel wires are welded from beginning to end, to guarantee continuous production with two groups of pay off racks.Steel wire is through the roller of mechanical descaling device, roller footpath D is 80mm, several 13 of roller, and roll spacing t is 75mm, roller is divided into three groups, as shown in Figure 1, three groups of roller axis are the space interlaced arrangement each other, and first group of roller is 6, roll axis is level, 4 roll axis of second group of roller and first group of roll axis are at 45,3 on the 3rd group of roller, and roll axis becomes 135 ° with first group of roll axis.Steel wire is gone into water flushing device through three groups of rollers are laggard, and the steel wire trend is opposite with water flushing direction, guarantees the quality of forcing flushing, 1.2 meters of effective length of flush.Steel wire enters the cathodic pickling groove immediately, pole plate is made with stereotype, its polarity arrangement as shown in Figure 6,1-3 is the anode cell body, the 4th is the negative electrode cell body, a cathodic pickling cell body has only a polarity, and the sulfuric acid solution in each cathodic pickling cell body is crossfire not mutually, and each cathodic pickling cell body has a style of one's own, sulfuric acid concentration 180 grams per liters, the pickling time is 10 seconds, and steel wire pickling time in the anode cell body is 7.5 seconds, and the pickling time is 2.5 seconds in the negative electrode cell body.15 meters of descaling bath length overalls, 50 amperes of current strength, anodic current density are 6A/dm 2, cathode-current density is 2A/dm 2, the Fe in the pickle + 2Concentration is controlled at below 200 grams per liters, and pickling temperature is less than 45 ℃.Place 4 pickling cell bodies at a big hopper, provide the circulation acid solution with a sour pump.Remove steel wire behind the surperficial firecoat through hot cleaner, steel wire is preheating to about 70 ℃, then to being coated with the boron groove, borax soln concentration is 300 grams per liters, pH value is 9.3, and the borax soln temperature is coated with 2.3 seconds boron time about 70 ℃, steel wire walking line speed is 90 meters/minute, is coated with 3.5 meters of boron slot lengths.The steel wire that coats borax carries out prestretching, adopts 550 single-head wire drawers, and pulling capacity is about 100 kilograms, draft about 20%.Enter admission machine at last, 90 meters/minute of take-up speeds.
The utility model advantage is:
1, metal wire material surface de-scaling, be coated with lubricant, wire drawing is consecutive production, automaticity height, labor productivity height, production cost are low;
2, the metal wire material surface de-scaling is clean;
3, basic non-environmental-pollution;
4, equipment investment is few, floor space is little.

Claims (2)

1, the continuous pretreatment unit of a kind of wire surface, form by flushed channel, descaling bath, rinse bath, painted groove, it is characterized in that: descaling bath is made up of hopper 4, bracket 5 and cathodic pickling cell body 6, cathodic pickling cell body 6 is made up of end face shrouding 7, pole plate 8, feed tube 9, leakage pipe 10 and pickling pipe 11, pickling pipe 11 top end openings, each cathodic pickling cell body 6 in the descaling bath is with a polarity, and pole plate 8 adopts opposed polarity, can be male or female.
2, the continuous pretreatment unit of wire surface according to claim 1 is characterized in that: painted groove is made up of liquid suction pipe 12, silk rolling mould 13, silk rolling groove 14, feed tube 15 and liquid storage tank 16.
CN 90214663 1990-10-26 1990-10-26 Continuous pretreatment device for wire material surface Withdrawn CN2095720U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 90214663 CN2095720U (en) 1990-10-26 1990-10-26 Continuous pretreatment device for wire material surface

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 90214663 CN2095720U (en) 1990-10-26 1990-10-26 Continuous pretreatment device for wire material surface

Publications (1)

Publication Number Publication Date
CN2095720U true CN2095720U (en) 1992-02-12

Family

ID=4894022

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 90214663 Withdrawn CN2095720U (en) 1990-10-26 1990-10-26 Continuous pretreatment device for wire material surface

Country Status (1)

Country Link
CN (1) CN2095720U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101961736A (en) * 2010-09-03 2011-02-02 宁波金田铜业(集团)股份有限公司 Continuous pickling and wiredrawing process of brass wire
CN103639196A (en) * 2013-12-26 2014-03-19 安徽工业大学 Efficient energy-saving manufacturing method for building-used cold rolling twisted steel
CN110319724A (en) * 2019-07-03 2019-10-11 江西华度电子新材料有限公司 A method of restoring liquid-sucking core capillary performance

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101961736A (en) * 2010-09-03 2011-02-02 宁波金田铜业(集团)股份有限公司 Continuous pickling and wiredrawing process of brass wire
CN103639196A (en) * 2013-12-26 2014-03-19 安徽工业大学 Efficient energy-saving manufacturing method for building-used cold rolling twisted steel
CN110319724A (en) * 2019-07-03 2019-10-11 江西华度电子新材料有限公司 A method of restoring liquid-sucking core capillary performance

Similar Documents

Publication Publication Date Title
CN1068389C (en) A hot-rolled steel strip manufacturing and descaling method and an apparatus thereof
CN104438391A (en) Automatic wire-welding surface treatment process and device for stainless steel
CN102765037A (en) Process method for removing oxide skin on surface of metal wire
CN2095720U (en) Continuous pretreatment device for wire material surface
JP2895502B2 (en) Metal fibers obtained by pulling a metal bundle
CN211199440U (en) Electroplating device for steel wire
CN215440744U (en) Device for preventing bubble from being left over for electroplating production of electronic component
CN112626598B (en) Continuous electroplating production line
CN114481247A (en) Tin plating equipment and tin plating process for contact wire
JP2975203B2 (en) Metal fiber manufacturing method
CN208261554U (en) Superfine micro- wire continuous ultrasound washing unit
CN202752982U (en) Metal wire surface scale eliminating device
CN208542667U (en) A kind of supersonic mould cleaning machine
CN111330998A (en) Production method of hot-galvanized steel wire for bridge cable
CN2183374Y (en) Ring-shape wire electroplating machine
CN214263283U (en) Practical wire drawing machine die holder
CN216399154U (en) Galvanized iron wire processing frock convenient to maintain
CN110860745A (en) Online cathode product removing method and device in micro-electrolysis linear cutting
CN220265796U (en) Surface treatment device for high-strength steel pipe
CN213164911U (en) Automatic assembly line sand blasting system for hot galvanizing
CN110983350A (en) Degreasing unit for eliminating scratch defects on surface of strip steel and strip steel degreasing process
CN212741560U (en) Galvanizing device for machine part production
CN217700700U (en) Prestressed steel strand production system
CN211757110U (en) Continuous belt cleaning device of full-automatic utmost point oxidation production line of environmental protection
CN213917275U (en) Numerical control machine tool equipment with cleaning function

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee