CN204589340U - A kind of super anti-corrosion nickel plating-chromium parts - Google Patents
A kind of super anti-corrosion nickel plating-chromium parts Download PDFInfo
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- CN204589340U CN204589340U CN201520136286.6U CN201520136286U CN204589340U CN 204589340 U CN204589340 U CN 204589340U CN 201520136286 U CN201520136286 U CN 201520136286U CN 204589340 U CN204589340 U CN 204589340U
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Abstract
The utility model relates to a kind of super anti-corrosion nickel plating-chromium parts, belongs to electroplating technology field.It comprises base material; Pre-treatment coating, its deposition over the whole substrate, pre-treatment coating is formed with copper plate; With half light nickel dam, it is formed on copper plate; With full light nickel dam or husky fourth nickel dam, it is formed at half light nickel dam; And functional layer, it is formed on full light nickel dam or husky fourth nickel dam, and wherein functional layer comprises low potential nickel dam and is formed at the micropore nickel dam on low potential nickel dam; And ornament layer, it is formed on micropore nickel dam.Potential difference between low potential nickel dam and micropore nickel dam is 10-120mv; Low potential nickel dam include one deck in high-sulfur nickel dam, tiny crack nickel dam or two-layer between compound, when adopting tiny crack and high-sulfur nickel composite deposite, between tiny crack and high-sulfur nickel, potential difference is 10-80mv.Both ensure the shiny appearance of parts micropore nickel dam, make it have again superelevation solidity to corrosion, hardness, wear resistance.
Description
Technical field
The utility model relates to a kind of workpiece with electroplating surface Rotating fields, particularly a kind of super anti-corrosion nickel plating-chromium parts.
In the application, potential difference is the difference of the normal potential integrally recorded separately with adjacent two layers.
Background technology
More and more tighter to environmental requirement of European market, and each automobile factory is more and more higher to the corrosion proof requirement of plating, the corrosion that current chromium plating cannot meet specific environment requires (reaching salt-fog resistant test 80h and resistance to Russian mud test 336h) simultaneously.
The method that in electroplating industry, the chromium plating again of double layer nickel or three layers of nickel is first plated in general application improves the antiseptic power of workpiece, the double layer nickel technique be widely used has: half light nickel+light nickel+flawless chromium, the three layers of nickel technique be widely used have: half light nickel+light nickel+microporous nickel+flawless chromium, or half light nickel+light nickel+micro-crack nickel+flawless chromium, but because the stress of layers of chrome self is large, industrially be difficult to obtain a kind ofly there is no the chromium electrolytic coating of crackle or hole (comprising sexavalent chrome and trivalent chromium coating) completely, expose after aerial chromium electrolytic coating is passivated, its current potential than nickel just, when running into corrosive medium, just corrosion cell is formed with nickel dam, cause the corrosion of nickel dam, excessive corrosion is there will be in extreme environment, the big area of surperficial layers of chrome is caused to come off, affect the quality of product.In order to improve the antiseptic power of coating further, microporous nickel and micro-crack nickel are applied on light nickel coating, its effect is by different plating technologies, product surface is impelled to produce a large amount of tiny cracks or micropore, form a large amount of small etching channels, thus hot spot is divided into the point that naked eyes can not identify, reduce coming off of layers of chrome, to reach the exterior quality improved in use procedure.Owing to being used alone microporous nickel or micro-crack nickel, be limited to corrosion proof raising; And tiny crack coordinates with trivalent chromium, there is the problems such as appearance poor, cause the product for high corrosion resistant requirement to there is inapplicability.Simultaneously in part prior art, disclose and change microporous nickel technique to reach noble potential characteristic, thus meet the requirement of trivalent chromium corrosion resistance nature, but this this Technology cannot realize and sexavalent chrome, trivalent chromium mixed production, and two kinds of parts all meet the corrosion-resistant requirement of high-quality.
In prior art, as Chinese patent application (publication number: CN 101988211A) relates to a kind of metallic surface multiple layer nickel plating technique with superior antiseptic property, electroplating technology flow process is: A. plastic part surface metallizes, B. bright copper, the bright nickel of C. half, D. high-sulfur nickel E. bright nickel, F. microporous nickel, G. washes, H. light chromium, I. wash, J. is dry; Although adopt these four layers of nickel nickel plating solutions to carry out at frosting electroplating the erosion resistance that improve plastic component to a certain extent in this technical scheme, but the resistance to corrosion of this technique still cannot reach containing deicer salts (CaCl
2) requirement of corrosive environment.And about introducing the technique of micro-crack nickel, as Chinese patent application (publication number: CN101705508A) relates to a kind of electroplate liquid for micro-crack nickel plating and application thereof, this micro-crack nickel electroplate liquid mainly composed as follows: nickelous chloride: 180-260 grams per liter, acetic acid: 20-60 milliliter/liter, ELPELYT MR:80-20 milliliter/liter, 62A:1-5 milliliter/liter, the evaluation physical constraints of the example described in patent documentation is sexavalent chrome plating, do not refer to trivalent chromium plating, enter checking simultaneously and there is poor corrosion resistance, outward appearance such as not to meet at the phenomenon.
Summary of the invention
Technical problem to be solved in the utility model is the present situation for prior art, and a kind of super anti-corrosion nickel plating-chromium parts are provided, by organically combining corrosion resistance characteristic and the chemical property of land productivity functional layer MULTI-LAYER NICKEL structure, both ensure that the shiny appearance characteristic of micropore nickel dam, have again and comprise microporous nickel, micro-crack nickel and or the multiple solidity to corrosion of functional layer of high-sulfur nickel dam, product can be made to reach superelevation solidity to corrosion, structural stability, hardness, wear resistance, even if after low potential nickel dam is corroded, micropore nickel dam, half light nickel dam, full light nickel dam or husky fourth nickel dam can play the effect of supporting and delaying to corrode equally.
The utility model solves the problems of the technologies described above adopted technical scheme: a kind of super anti-corrosion nickel plating-chromium parts, and these super anti-corrosion nickel plating-chromium parts comprise:
Base material; Here the utility model base material can adopt metal, plastics and other can be suitable for the parts of plating;
(pre-treatment coating can comprise the arbitrary or two-layer compound in electroless nickel layer or bottoming nickel dam to pre-treatment coating, on base material, there is not this layer yet, concrete selection is depending on the material of base material, when electroless nickel layer and bottoming nickel dam exist simultaneously, then electroless nickel layer is formed on base material, bottoming nickel dam is formed in electroless nickel layer), its deposition over the whole substrate, pre-treatment coating is formed with copper plate; With
Half light nickel dam, it is formed on copper plate; With
Full light nickel dam or husky fourth nickel dam, it is formed at half light nickel dam; With
Functional layer, it is formed on full light nickel dam or husky fourth nickel dam, and wherein functional layer comprises low potential nickel dam and is formed at the micropore nickel dam on low potential nickel dam; With
Ornament layer, it is formed on micropore nickel dam, described ornament layer is the arbitrary of trivalent chromium coating or sexavalent chrome coating, and wherein trivalent chromium coating can be the trivalent chromium coating of the white chromium coating of trivalent or trivalent black chromium plating or other kind, and trivalent chromium coating surface also can contain passive film.
The measure taked for optimizing such scheme specifically comprises:
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, the potential difference between described micropore nickel dam and low potential nickel dam is within the scope of 10-120mv.
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, described low potential nickel dam include one deck in high-sulfur nickel dam, tiny crack nickel dam or two-layer between composite deposite.
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, the potential difference between described micropore nickel dam and low potential nickel dam is within the scope of 20-100mv.
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, when low potential nickel dam adopts the composite deposite of tiny crack nickel dam and high-sulfur nickel dam, between tiny crack nickel dam and high-sulfur nickel dam, potential difference is in 10-80mv.Here when corroding arrival low potential nickel dam, because the current potential of tiny crack nickel dam is higher than the current potential of high-sulfur nickel dam, now high-sulfur nickel dam is preferentially corroded by as anodic coating again, extends the corrosion of tiny crack nickel dam, thus improves corrosion-resistant degree further.
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, described full light nickel dam or the potential difference between husky fourth nickel dam and low potential nickel dam are within the scope of 0-100mv.
In the super anti-corrosion nickel plating-chromium parts of above-mentioned one, the potential difference between described half light nickel dam and full light nickel dam or husky fourth nickel dam is within the scope of 100-200mv.
Disclosed in the utility model, the manufacture method of super anti-corrosion nickel plating-chromium parts comprises the steps:
Pre-treatment is carried out on the surface of base material;
Pre-treatment coating is deposited over the whole substrate, and copper plate is formed on pre-treatment coating; With
Half light nickel dam is formed on copper plate; With
Full light nickel dam or husky fourth nickel dam are formed at half light nickel dam; With
Low potential layer in functional layer is formed on full light nickel dam or husky fourth nickel dam; With
Micropore nickel dam in functional layer is formed on low potential nickel dam; Potential difference between described micropore nickel dam and low potential nickel dam is 10-120mv, potential difference is controlled, within the scope of this, in electroplating process, not easily to occur bubbling, and coating structure is more stable firmly simultaneously, separation not easily occurs and peels off;
Ornament layer is formed on micropore nickel dam.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, described low potential nickel dam include one deck in high-sulfur nickel dam, tiny crack nickel dam or two-layer between compound.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, described micropore nickel dam adopts the plating of plating microporous nickel plating solution to form, described plating microporous nickel plating solution comprises composition and concentration is: aqueous sulfuric acid nickel 300-350g/L, moisture nickelous chloride 50-60g/L, boric acid 40-50g/L, nickel envelope brightening agent 6-12ml/L (be sure of that the chemical trade (Shanghai) Co., Ltd. of happy think of thinks hereinafter referred to as happy, wheat dolantin science and technology (Suzhou) company limited is hereinafter referred to as wheat dolantin, NIMAC 14INDEX as happy 63 and the wheat dolantin thought), nickel envelope key light agent 4-7.5ml/L (610CFC thought as happy and the NIMAC 33 of wheat dolantin), nickel envelope particle 0.2-1.5g/L (ENHANCER thought as happy and the NiMac Hypore XL dispersion agent of wheat dolantin), nickel envelope particle dispersants 0.5-3ml/L, wetting agent 1-5ml/L.When micropore nickel dam is coated with, service temperature controls between 50-60 DEG C, pH value controls between 3.8-4.6, and current density is 2-5ASD, and the operating time controls between 2-8min, make nickel deposition on plated item by the mode of direct current electrolysis, microporous nickel layer thickness is not less than 1.5 microns.Plating microporous nickel refers to and plates one deck uniformly containing the coating of numerous non-conductive particulate at substrate surface, disperses corrosion current further, reduces corrosion electric current density, improve coating corrosion stability comprehensively.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, described tiny crack nickel dam adopts the plating of plating micro-crack nickel plating solution to form, described micro-crack nickel plating solution comprises composition and concentration is: moisture nickelous chloride: 180-260g/L, acetic acid: 20-60ml/L, PN-1A:40-90g/L, PN-2A:1-5ml/L, wetting agent: 1-5ml/L.Service temperature controls between 25-35 DEG C, pH value controls between 3.6-4.6, and current density is 5-9ASD, and the operating time controls between 2-5min, make nickel deposition at the full light nickel dam of nickel plating-chromium parts on the surface by the mode of direct current electrolysis, require that micro-crack nickel layer thickness is not less than 1.5 microns.Plating micro-crack nickel refer to substrate surface plate one deck all and the coating containing numerous crackle, dispersion corrosion current, reduces corrosion electric current density.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, described high-sulfur nickel dam adopts the plating of plating high-sulfur nickel plating bath to form, described high-sulfur nickel plating bath comprises composition and concentration is: aqueous sulfuric acid nickel 250-350g/L, moisture nickelous chloride 35-60g/L, boric acid 35-65g/L, high sulfur additives 3-10ml/L, wetting agent 0.5-3ml/L.Wetting agent is as the happy 62A of think of and the NIMAC 32C WETTER of wheat dolantin.Service temperature controls between 55-65 DEG C, pH is to controlling between 2.0-3.5, current density is 2-6ASD, operating time controls between 2-8min, make nickel deposition at parts full light nickel dam or husky fourth nickel dam on the surface by the mode of direct current electrolysis, described high-sulfur nickel coating thickness is not less than 1.0 microns.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, half described light nickel dam adopts the plating of plating half light nickel plating bath to form, described half light nickel plating bath comprises composition and concentration is: aqueous sulfuric acid nickel 200-300g/L, moisture nickelous chloride 35-50g/L, boric acid 35-50g/L, the elementary brightening agent 3.0-7.0ml/L of half light nickel (the BTL MU thought as happy and the NIMAC SF DUCT of wheat dolantin), half light nickel second-class brightener 0.3-1.0ml/L (TL-2 thought as happy and the NIMAC SF LEVELER of wheat dolantin), potential difference adjusting agent 0.1-0.6ml/L (the B benefit thought as happy and the NIMAC SF MAINTENANCE of wheat dolantin), wetting agent 1.0-3.0ml/L (62A thought as happy and the NIMAC 32C WETTER of wheat dolantin).Service temperature controls between 50-60 DEG C, pH value controls between 3.6-4.6, and current density is 2-5ASD, and the operating time controls between 12-24min, make nickel deposition at nickel plating-chromium parts copper plate on the surface by the mode of direct current electrolysis, described half light nickel layer thickness is not less than 8 microns.
In the manufacture method of above-mentioned a kind of super anti-corrosion nickel plating-chromium parts, full light nickel dam adopts the full light nickel plating bath plating of plating to form, described full light nickel plating bath comprises composition and concentration is: aqueous sulfuric acid nickel 240-360g/L, moisture nickelous chloride 35-65g/L, boric acid 35-65g/L, bright nickel softening agent 8-15ml/L (the NIMAC 14INDEX as happy 63 and the wheat dolantin thought), bright nickel brightening agent A 5-10ml/L (610CFC thought as happy and the NIMAC 33 of wheat dolantin), bright nickel key light agent 0.5-0.9ml/L (66E thought as happy and the NiMac Chanllenger Plus of wheat dolantin), wetting agent 1.0-3.0ml/L (62A thought as happy and the NIMAC 32C WETTER of wheat dolantin).Service temperature controls between 50-60 DEG C, pH value controls between 3.6-4.6, and current density is 2-5ASD, and the operating time controls between 9-20min, make nickel deposition at nickel plating-chromium parts half light nickel dam on the surface by the mode of direct current electrolysis, described full light nickel layer thickness is not less than 5 microns.
In the manufacture method of above-mentioned super anti-corrosion nickel plating-chromium parts, husky fourth nickel dam adopts the husky fourth nickel plating bath plating of plating to form, described husky fourth nickel plating bath comprises composition and concentration is: aqueous sulfuric acid nickel 250-350g/L, moisture nickelous chloride 35-60g/L, boric acid 35-65g/L, supplementary additive 5-20ml/L (the Elpelyt pearlbrite carrier K4 thought as happy and Elpelyt carrier brightener H), husky fourth nickel forming agent 0.1-0.6ml/L (as the happy Elpelyt pearlbrite additive K6AL thought).
When in basal layer being half light nickel dam, full light nickel dam, plate solution composition in half light nickel, full light nickel the same, additive is different, thus make the coating structure of formation different, make each step all play different effects, half light nickel dam can improve the erosion resistance of coating, full light nickel dam can improve the luminance brightness of coating, plate half light nickel and refer to the nickel dam plating one deck half light at nickel plating-chromium parts surface, half light nickel dam is columnar structure, can improve the erosion resistance of coating.Plate full light nickel and refer to the nickel dam plating one deck entire bright at nickel plating-chromium parts surface, full light nickel dam is laminate structure, can improve the luminance brightness of coating.
In the manufacture method of above-mentioned super anti-corrosion nickel plating-chromium parts, also comprise base material pretreatment process in early stage, at least include surperficial grease treatment process, surface hydrophilic, surface coarsening treatment process, surperficial neutralizing treatment operation, surperficial preimpregnation, surface activation process operation and surperficial dispergation treatment process comprising ABS resin at interior non-metal kind base material pretreatment process in early stage; Metal species base material then can carry out follow-uply being coated with work after surperficial grease treatment process carries out oil removing, the corresponding operation of the non-metallic base being suitable for following statement equally in earlier stage in pretreatment process.
In the manufacture method of above-mentioned super anti-corrosion nickel plating-chromium parts, non-metal kind base material pretreatment process in early stage is specially and base material blank is cleaned degrease in sodium hydroxide, sodium carbonate and water glass mixing solutions, immerse after degrease in chromic trioxide and sulfuric acid mixture liquid and carry out surface coarsening process, then put into hydrochloric acid soln and carry out surface neutralization, adopt colloidal palladium solution to carry out surface activation process after neutralization, then in sulphuric acid soln, carry out surperficial dispergation process.
As preferably, the mixing solutions of surperficial grease treatment process comprises composition and concentration is: the concentration of sodium hydroxide is 20-50g/L, and the concentration of sodium carbonate is 10-40g/L, and the concentration of water glass is 10-40g/L, tensio-active agent 1-3g/L.
Here surperficial degrease step can remove greasy dirt and other impurity of substrate surface, impels surface coarsening even, improves binding force of cladding material.
As preferably, the sulphuric acid soln concentration of surface hydrophilic operation is 20-100g/L, whole agent 0.5-2ml/L.
As preferably, the mixed solution of surface coarsening treatment process comprises composition and concentration is: the concentration of chromic trioxide is 330-480g/L, and the concentration of sulfuric acid is 330-480g/L.
Here chromic trioxide is the main salt in plating solution, chromium metal and production chromium sesquioxide hydrate etc. is deposited at substrate surface by the mechanism of oxidation-reduction reaction and electron exchange, coating is turned black, the covering power of chromic trioxide to plating solution has considerable influence, if chromic trioxide content is high, then covering power is strong, crystallization is careful, if but chromic trioxide too high levels, the hardness of coating then can be made to decline, in addition, chromic trioxide and sulfuric acid can at corrosion substrate surface to form micro-roughened surface at substrate surface as etching reagent, " snap close effect " required during to guarantee electroless plating, the bonding force of substrate surface and coating is improved with this.But sulfate radical can reduce the color characteristics of coating, coating is turned to be yellow, in order to can reach corrosion substrate surface and reduce harmful effect simultaneously, need the content of accurately configuration sulfuric acid.
As preferably, in surface and the concentration of hydrochloric acid solution of operation be 30-100ml/L, hydrazine hydrate 15-60ml/L.
As preferably, the concentration of hydrochloric acid solution of surperficial preimpregnation operation is 40-120ml/L.
As preferably, the colloidal palladium solution of surface activation process comprises composition and concentration is: the concentration of Palladous chloride is the concentration 1-6g/L of 20-60ppm, tin protochloride, hydrochloric acid 180-280ml/L.
Here in colloidal palladium solution, Palladous chloride is covered in substrate surface, for follow-up chemical nickel provides catalytic center, the tin ion of tin protochloride then can be deposited on around palladium ion with chemical combination group too, avoid palladium ion be oxidized in water or in air and come off, the life cycle of colloidal palladium solution can be increased.
As preferably, the sulphuric acid soln concentration of surperficial dispergation treatment process is 40-100g/L.
Surface dispergation process refers to and utilizes sulfuric acid to remove in colloidal palladium solution the tin protochloride be coated on around palladous oxide, is come out by palladium metal particle, makes subsequent chemistry sink nickel technique more smooth and easy.
As preferably, the electroless nickel layer plating solution of electroless nickel layer operation comprises composition and concentration is: the concentration of single nickel salt is 15-40g/L, and the concentration of sodium hypophosphite is 20-50g/L, the concentration of Trisodium Citrate is 10-4g/L, ammonium chloride 10-50g/L, ammoniacal liquor, PH regulates use, PH=8.6-9.2.
As preferably, the bottoming nickel plating bath of plating bottoming nickel operation comprises composition and concentration is: the concentration of aqueous sulfuric acid nickel is 180-280g/L, and the concentration of moisture nickelous chloride is 35-60g/L, and the concentration of boric acid is 35-60g/L, wetting agent 1-3ml/L.
When electroless nickel layer and bottoming nickel dam exist on matrix simultaneously, matrix in chemical sinking nickel, after making substrate surface cover the nickel dam of the conduction of layer by redox reaction; And in plating bottoming nickel, then adopt electrochemical method in chemical nickel, plate one deck nickel, strengthen the electroconductibility of coating further.In this step, aqueous sulfuric acid nickel, moisture nickelous chloride provide nickel ion needed for electrochemical reaction.
As preferably, in the copper plate plating solution of copper plate operation, each component and concentration are: the concentration of copper sulfate is 160-260g/L, and the concentration of sulfuric acid is 50-100g/L, chlorion is 40-100ppm, leveling agent 0.2-1ml/L, walk agent 0.2-1ml/L, open cylinder agent 2-10ml/L.
Here the object of copper plate utilizes the characteristic of copper sulfate to improve luminance brightness and the planarization of substrate surface, and can also improve the toughness of coating entirety.This is because copper coating compares nickel coating and other metal plating, its ductility is better, and after therefore plating sour layers of copper, toughness and the Surface flat of overall coating are improved.
Wherein, in the utility model nickel plating-chromium parts, when low potential nickel dam adopt independent tiny crack nickel dam or for high-sulfur nickel dam and tiny crack nickel dam composition compound nickel dam, the anticorrosion effect that the utility model reaches best can be made, here tiny crack nickel dam in functional layer, micropore nickel dam or both combine can play protection against corrosion and protection base material reason be, on workpiece, coated metal/substrate metal extremely easily forms corrosion cell, when anode and cathode current potential is determined, its erosion rate controlled by the ratio of coated metal (negative electrode) surface substrate metal (anode) exposed area.When only having the hot spot at a place, at this moment cathode/anode ratio is maximum, corrosion current just concentrates on this point, erosion rate just becomes very large, easily inwardly forms pitting, but when metal coating surface exists more potential hot spot, cathode/anode ratio is less, corrosion current is assigned to everywhere, and the electric current originally in hot spot significantly reduces, and erosion rate also reduces greatly.Meanwhile, due to the segmentation between micropore or crackle, coating negative electrode is formed discontinuous, the coating after divided becomes small area by big area, further limit so again cathode/anode ratio.But along with time the passing of asking; when coating surface be subject to extraneous factor impact start to occur large mode-Ⅲ crack time; the potential corrosion cell of tiny crack, microvoid structure will be initiated; thus it is subject to the effect of hot spot to protection; thus just can play double-core and reduce the effect of corrosion electric current density, thus the corrosion-resistant degree of significant increase.
The anticorrosive mechanism of low potential nickel
The first step: when piece surface removes corrosive medium, because ornament layer (such as layers of chrome) exists the passivation layer of highly corrosion resistant, the micropore on layers of chrome surface exists, the nickel dam of corrosion at micropore place is guided to launch, due to the discontinuity of micropore, cause when corroding total amount and being constant, corrosion is separated into numerous regions, therefore corrodes and carries out not affecting under apparent condition.。
Second step: when corroding arrival low potential nickel dam, because microporous nickel current potential is higher than low potential nickel current potential, now low potential nickel is preferentially corroded as anodic coating (namely low potential nickel dam is preferentially as sacrifice layer), and the corrosion in microporous nickel is terminated.Under the effect of a large amount of discontinuous tiny crack, guide corrosion in crackle depth and laterally launch simultaneously; the nickel dam area corroded will increase and discontinuous greatly; when corrosion current is certain; these " micropores " have disperseed corrosion current greatly; again reduce single-point erosion rate; the corrosion speed delayed, protect the layers of chrome in appearance and adhesion layer micropore nickel dam thereof, product surface corrosion resistance improves further simultaneously.
3rd step: when to corrode in low potential nickel dam further to downward-extension, because below low potential nickel dam, the current potential of coating (as copper plate) is higher than low potential nickel equally, low potential nickel has been regarded anodic coating equally, corrosion now to downward-extension is terminated, corrosion position laterally carries out in low potential nickel, delay so again the time of corroding to base material further, greatly fall at the end speed of corrosion.
Compared with prior art, the utility model has the advantage of:
1, the high-sulfur nickel dam in the double-core method MULTI-LAYER NICKEL of the utility model substrate surface i.e. half light nickel dam, full light nickel dam or husky fourth nickel dam, low potential nickel dam and or tiny crack nickel dam, micropore nickel dam, there is high Corrosion Protection, high rigidity, high-wearing feature, binding force of cladding material is good, luminance brightness advantages of higher, the utility model substrate surface electroplates the micropore nickel dam and low potential nickel dam that obtain, has high Corrosion Protection, high rigidity, high-wearing feature, binding force of cladding material is good, luminance brightness advantages of higher; Simultaneously there is the micropore nickel dam of noble potential characteristic and there is the MULTI-LAYER NICKEL of low potential characteristic---low potential nickel dam is for functional layer, and with low potential nickel dam for sacrifice layer, micro-electric current of galvanic corrosion can be disperseed with the micropore nickel dam with microvoid structure, delay be corroded generation, formed simultaneously and can also form oxide compound support after oxidation by microvoid structure, after can being subject to comparatively serious corrosion at the low potential nickel dam as sacrifice layer, it is formed and support, reduce part coating damage speed.The low potential nickel dam as sacrifice layer arranged has lower electromotive force; when the generation galvanic corrosion of piece surface coating; low potential nickel dam preferentially corrodes; and when there is micropore nickel dam or tiny crack nickel dam; its micropore or micro-cracked structure can play the micro-electric current of dispersion corrosion equally; when also having a layer structure outside low potential nickel dam, (during as ornament layer or protective layer) can also be supported outboard structure by micropore or micro-cracked structure, the steadiness of strongthener structure simultaneously.The utility model scheme utilizes the pore texture of microporous nickel and micro-crack nickel in addition, while strongthener structural support performance, can also play the effect reducing quality of coating and expend with reduction raw material.Its micro hole structure can also form large-area sull structure when there is oxidation corrosion simultaneously, thus greatly delays the generation of corrosion.
Accompanying drawing explanation
Fig. 1 is the coating structure schematic diagram of an embodiment of the utility model nickel plating-chromium parts.
Nickel plating-chromium parts CASS metallograph after 72 hours of Fig. 2 prior art, in Fig. 2, (a) is the front metallograph of sample after experiment, and in Fig. 2, (b) is side (section) metallograph of sample after experiment.
Fig. 3 the utility model nickel plating-chromium parts CASS metallograph after 72 hours, in Fig. 3, (a) is the front metallograph of sample after experiment, and in Fig. 3, (a) is the side metallograph of sample after experiment.
The picture carried out after 168 and 336 hours tested by the nickel plating-chromium parts fluorgypsum of Fig. 4 prior art.
The picture carried out after 168 and 336 hours tested by Fig. 5 the utility model nickel plating-chromium parts fluorgypsum.
Fig. 6 the utility model compound low potential nickel dam potential difference picture (low potential nickel dam is the composite bed of high-sulfur nickel dam and tiny crack nickel dam).
Fig. 7 the utility model list low potential nickel dam potential difference picture (low potential nickel dam is the arbitrary of high-sulfur nickel dam or tiny crack nickel dam).
Fig. 8 MULTI-LAYER NICKEL corrosion principle of the present utility model figure (taking ABS as part base material).
Reference numerals list:
1, base material; 2, pre-treatment coating; 21, vacancy is corroded; 3, copper plate; 31, surface micropore; 32, corrosion hole; 4, functional layer; 141, low potential nickel dam; 142, micropore nickel dam; 62, half light nickel dam; 61, full light nickel dam or husky fourth nickel dam; 801, corrosive medium; 802, ornament layer; 805, erosional surface; 808, bottoming nickel dam; 809, electroless nickel layer; 810, ABS substrate.
Embodiment
Below in conjunction with the drawings and specific embodiments, illustrate the utility model further, following embodiment should be understood and be only not used in restriction scope of the present utility model for illustration of the utility model.
In the utility model embodiment, the solvent of solution is water (including, without being limited to distilled water, deionized water, low-hardness water etc.) unless otherwise indicated.
As shown in Figure 1, below the coating structure of the utility model nickel plating parts is described.
Constructive embodiment 1
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, bottoming nickel dam 808, and electroless nickel layer 809 is deposited on whole base material 1, and bottoming nickel dam 808 is deposited in electroless nickel layer 809, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is high-sulfur nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is the white chromium coating of trivalent.
Constructive embodiment 2
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, bottoming nickel dam 808, and electroless nickel layer 809 is deposited on whole base material 1, and bottoming nickel dam 808 is deposited in electroless nickel layer 809, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is tiny crack nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is trivalent black chromium plating.
Constructive embodiment 3
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, bottoming nickel dam 808, and electroless nickel layer 809 is deposited on whole base material 1, and bottoming nickel dam 808 is deposited in electroless nickel layer 809, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, wherein low potential nickel dam 141 is tiny crack nickel dam, it is formed at full light nickel dam 61, and for high-sulfur nickel dam and tiny crack nickel dam, (can be that high-sulfur nickel dam is formed on full light nickel dam or husky fourth nickel dam 5, tiny crack nickel dam be formed on high-sulfur nickel dam; Also can be that tiny crack nickel dam is formed on full light nickel dam or husky fourth nickel dam 5, high-sulfur nickel dam be formed on tiny crack nickel dam); With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is trivalent black chromium plating.
Constructive embodiment 4
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, and electroless nickel layer 809 is deposited on whole base material 1, and electroless nickel layer 809 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is high-sulfur nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is the white chromium coating of trivalent.
Constructive embodiment 5
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, and electroless nickel layer 809 is deposited on whole base material 1, and electroless nickel layer 809 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is tiny crack nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is sexavalent chrome coating.
Constructive embodiment 6
Base material 1 (ABS material); Pre-treatment coating 2 comprises electroless nickel layer 809, and electroless nickel layer 809 is deposited on whole base material 1, and electroless nickel layer 809 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, wherein low potential nickel dam 141 is tiny crack nickel dam, it is formed at full light nickel dam 61, and for high-sulfur nickel dam and tiny crack nickel dam, (can be that high-sulfur nickel dam is formed on full light nickel dam or husky fourth nickel dam 5, tiny crack nickel dam be formed on high-sulfur nickel dam; Also can be that tiny crack nickel dam is formed on full light nickel dam or husky fourth nickel dam 5, high-sulfur nickel dam be formed on tiny crack nickel dam); With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is sexavalent chrome coating.
Constructive embodiment 7
Base material 1 (ABS material); Pre-treatment coating 2 comprises bottoming nickel dam 808, and electroless nickel layer 808 is deposited on whole base material 1, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is high-sulfur nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is trivalent black chromium plating.
Constructive embodiment 8
Base material 1 (ABS material); Pre-treatment coating 2 comprises bottoming nickel dam 808, and electroless nickel layer 808 is deposited on whole base material 1, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, and wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, and wherein low potential nickel dam 141 is tiny crack nickel dam, and it is formed on full light nickel dam 61; With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is trivalent black chromium plating, and trivalent black chromium plating surface is containing passive film.
Constructive embodiment 9
Base material 1 (ABS material); Pre-treatment coating 2 comprises bottoming nickel dam 808, and electroless nickel layer 808 is deposited on whole base material 1, and bottoming nickel dam 808 is formed copper plate 3; Half light nickel dam 62, it is formed on copper plate 3; With full light nickel dam 61, it is formed on half light nickel dam 62; With functional layer 4, it is formed on full light nickel dam 61, wherein functional layer 4 comprises low potential nickel dam 141 and the micropore nickel dam 142 be formed on low potential nickel dam, wherein low potential nickel dam 141 is tiny crack nickel dam, it is formed at full light nickel dam 61, and for high-sulfur nickel dam and tiny crack nickel dam, (can be that high-sulfur nickel dam is formed on full light nickel dam 5, tiny crack nickel dam be formed on high-sulfur nickel dam; Also can be that tiny crack nickel dam is formed on full light nickel dam 5, high-sulfur nickel dam be formed on tiny crack nickel dam); With ornament layer 802, it is formed on micropore nickel dam 142, and ornament layer 802 is the white chromium coating of trivalent, and the white chromium coating surface of trivalent is containing passive film.
Unique difference of constructive embodiment 10-18 and constructive embodiment 1-9 is only: full light nickel dam 5 is husky fourth nickel dam 5.
Unique difference of constructive embodiment 19-36 and constructive embodiment 1-18 is only: base material 1 is nylon material.
Unique difference of constructive embodiment 37-54 and constructive embodiment 1-18 is only: base material 1 is pvc material.
Unique difference of constructive embodiment 55-72 and constructive embodiment 1-18 is only: base material 1 is pc material.
Unique difference of constructive embodiment 73-90 and constructive embodiment 1-18 is only: base material 1 is pet material.
Unique difference of constructive embodiment 91-108 and constructive embodiment 1-18 is only: base material 1 is bakelite material.
Unique difference of constructive embodiment 109-126 and constructive embodiment 1-18 is only: base material 1 is cast iron (including, without being limited to grey cast iron, white cast iron, spheroidal graphite cast iron, vermicular cast iron, malleable iron and cast alloy iron etc.) material.
Unique difference of constructive embodiment 127-144 and constructive embodiment 1-18 is only: base material 1 is steel (comprising various ordinary steel, stainless steel etc.) and aluminum alloy material, magnesium alloy material.
Base material 1 material adopted in technical solutions of the utility model can also may be used for being coated with on its surface the material of copper, nickel, chromium coating for other.
In the utility model embodiment, the solvent of solution is water (including, without being limited to distilled water, deionized water, low-hardness water etc.) unless otherwise indicated, and concentration is all with the solution measures of unit volume or quality.
The base material of following examples part preferably adopts ABS material.
Preparation embodiment 1-5
The manufacture method of the nickel plating parts of a kind of embodiment of the utility model is as follows, the surface of base material is carried out pre-treatment (pre-treatment in turn includes the following steps: surperficial degrease, surface hydrophilic process, surface coarsening process, surperficial neutralizing treatment, preimpregnation, surface activation process, surperficial dispergation process); Pre-treatment coating (is comprised chemical sinking nickel and bottoming nickel, the selection that whether pre-treatment coating retains and pre-treatment coating forms in addition is selected flexibly according to base material material and handicraft product demand) deposition is over the whole substrate, the electroless nickel layer outwards formed in turn by substrate surface and bottoming nickel dam, and copper plate is formed on pre-treatment coating (bottoming nickel dam is outer); With half light nickel dam is formed on copper plate; Half light nickel dam is formed at by full light nickel dam; With the low potential layer in functional layer is formed on copper plate, low potential nickel dam is high-sulfur nickel dam here; With the micropore nickel dam in functional layer is formed on high-sulfur nickel dam; Ornament layer is formed on micropore nickel dam.
Wherein, described micropore nickel dam and the potential difference between low potential nickel dam be respectively 20,30,40,50,60,10,80,90, other arbitrary values within the scope of the arbitrary or 20-100mv of 100mv (embodiment 1-5 can select in 20-100mv respectively (as 20,40,60,80,100mv) different numerical value is potential difference in corresponding embodiment between micropore nickel dam and low potential nickel dam, the potential difference in each embodiment between micropore nickel dam with low potential nickel dam also can be identical).
Described full light nickel dam and the potential difference between low potential nickel dam be respectively 0,10,20,30,40,50,60,10,80,90, other arbitrary values within the scope of the arbitrary or 0-100mv of 100mv (embodiment 1-5 can select in 0-100mv respectively (as 0,30,60,80,100mv) different numerical value is full potential difference between light nickel dam and low potential nickel dam in corresponding embodiment, in each embodiment, full potential difference between light nickel dam with low potential nickel dam also can be identical).
Potential difference between described half light nickel dam and full light nickel dam is respectively 100,110,120,130,140,150,160,170,180,190, other arbitrary values within the scope of the arbitrary or 100-200mv of 200mv (embodiment 1-5 can select in 100-200mv respectively (as 100,120,150,180,200mv) different numerical value is potential difference in corresponding embodiment between half light nickel dam and full light nickel dam, the potential difference in each embodiment between half light nickel dam with full light nickel dam also can be identical).
On above-mentioned nickel plating-chromium parts, the method for electronickelling comprises the steps:
(1) surperficial degrease: at sodium hydroxide NaOH, sodium carbonate Na
2cO
3with water glass Na
2siO
3clean in mixing solutions.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table one:
Table one:
(2) surface hydrophilic operation: at sulfuric acid H
2sO
4carry out with in whole agent.In this step, whole agent and sulfuric acid H
2sO
4concentration proportioning is in different embodiments in table two:
Table two:
(3) surface coarsening process: at chromic trioxide CrO
3with sulfuric acid H
2sO
4carry out in mixed solution.In this step, chromic trioxide CrO
3with sulfuric acid H
2sO
4concentration proportioning is in different embodiments in table three:
Table three:
(4) surperficial neutralizing treatment: the parts after surface coarsening process are put into hydrochloric acid soln and carries out.In this step, hydrochloric acid soln at the concentration proportioning of different embodiment in table four:
Table four:
(5) surperficial preimpregnation operation: the parts after surperficial neutralizing treatment are put into hydrochloric acid soln and carries out.In this step, hydrochloric acid soln at the concentration proportioning of different embodiment in table five:
Table five:
(6) surface activation process: surface activation process adopts colloidal palladium solution, colloidal palladium Chlorine in Solution palladium PdCl
2with tin protochloride SnCl
2at the concentration proportioning of different embodiment in table six:
Table six:
(7) surperficial dispergation process: at sulfuric acid H
2sO
4carry out in solution.In this step sulphuric acid soln at the concentration proportioning of different embodiment in table seven:
Table seven:
(8) chemical sinking nickel: containing sulfuric acid nickel
2sO
4-6H
2o, inferior sodium phosphate NaH
2pO
3-H
2o and Trisodium Citrate C
6h
5na
3o
7carry out in mixing solutions.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table eight:
Table eight:
(9) bottoming nickel is plated: containing aqueous sulfuric acid nickel
2sO
4-6H
2o, moisture nickelous chloride NiCl
2-6H
2o, boric acid H
3bO
3mixing solutions in carry out.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table nine:
Table nine:
(10) copper plate: at copper sulfate CuSO
4with sulfuric acid H
2sO
4carry out in mixing solutions.Copper sulfate CuSO
4with sulfuric acid H
2sO
4at the concentration proportioning of different embodiment in table ten:
Table ten:
(11) half light nickel dam is plated: containing sulfuric acid nickel
2sO
4-6H
2o, nickelous chloride NiCl
2--6H
2o, boric acid H
3bO
3mixing solutions in carry out.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table ten one; Plate other parameters in half light nickel operation in table ten two:
Table ten one:
Table ten two:
(12) full light nickel dam is plated: containing sulfuric acid nickel
2sO
4-6H
2o, moisture nickelous chloride NiCl
2-6H
2o, boric acid H
3bO
3mixing solutions in carry out.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table ten three; Plate other parameters in full light nickel operation in table ten four:
Table ten three:
Table ten four:
(13) high-sulfur nickel dam (low potential nickel dam), plating micropore nickel dam is plated successively.Wherein plate in the processing step of microporous nickel, high-sulfur nickel, the main component of plating solution is the same, is aqueous sulfuric acid nickel
2sO
4-6H
2o, moisture nickelous chloride NiCl
2-6H
2o and boric acid H
3bO
3mixing solutions.Plate high-sulfur nickel and plate the concentration proportioning of microporous nickel in different embodiment respectively in table ten five and table ten seven, nickel envelope brightening agent is 63 of happy think of here; The agent of nickel envelope key light is the happy 610CFC thought; Nickel envelope particulate vector is the happy ENHANCER thought; Wherein, plating high-sulfur nickel and other parameters in plating microporous nickel operation are respectively in table ten six and table ten eight:
Table ten five:
Table ten six:
Table ten seven:
Table ten eight:
(14) ornament layer is plated: carry out in the mixing solutions containing chromium chloride, potassium formiate.In this step, in mixing solutions, each component concentration proportioning is in different embodiments in table ten nine:
Table ten nine:
Preparation embodiment 6-10 is only with unique difference of preparation embodiment 1-5, and low potential nickel dam is fine fisssure lamina, and tiny crack nickel dam plating solution adopts plating solution as shown in following table 20 accordingly, and other parameters in plating micro-crack nickel operation are in table two 11:
Table two ten:
Table two 11:
Preparation embodiment 11-15 is only with unique difference of preparation embodiment 1-5, low potential nickel dam include high-sulfur nickel dam (each embodiment plating solution is accordingly in turn see shown in table ten five), tiny crack nickel dam (each embodiment plating solution is accordingly in turn see shown in table two ten) two-layer between compound.Wherein, described tiny crack nickel dam and the potential difference between high-sulfur nickel dam be respectively 10,20,30,40,50,60,10, other arbitrary values within the scope of the arbitrary or 10-80mv of 80mv (embodiment 11-15 can select in 10-80mv respectively (as 10,20,40,60,80mv) different numerical value is potential difference in corresponding embodiment between tiny crack nickel dam and high-sulfur nickel dam, the potential difference in each embodiment between tiny crack nickel dam with high-sulfur nickel dam also can be identical).
Preparation embodiment 16-30 is only with unique difference of preparation embodiment 1-15, and full light nickel dam is replaced to husky fourth nickel dam, and husky fourth nickel dam plating solution adopts plating solution (arbitrary numbering embodiment respective value) as shown in following table 22 accordingly.
Table two 12:
Preparation embodiment 31-60 is only with unique difference of preparation embodiment 1-30, white for trivalent in ornament layer layers of chrome is replaced to trivalent black chromium coating, and trivalent black chromium coating plating solution adopts plating solution (arbitrary numbering embodiment respective value) as shown in following table 23 accordingly.
Table two 13:
Preparation embodiment 61-90 is only with unique difference of preparation embodiment 1-30, white for trivalent in ornament layer layers of chrome is replaced to sexavalence layers of chrome, and sexavalence layers of chrome plating solution adopts plating solution (arbitrary numbering embodiment respective value) as shown in following table 24 accordingly.
Table two 14:
More than prepare PN-1A, PN-2A in embodiment and be Atotech (China) Chemical Co., Ltd. commercially available prod.
Comprehensive above all embodiments, can find out, the all embodiments of technical solutions of the utility model reach 96-120h and above (prior art then proposes as 40-48h) by CASS experiment, fluorgypsum experiment then reaches stable more than 336h (product that prior art obtains is then unstable, cannot carry out quantization signifying).
In technical solutions of the utility model, base material can also adopt materials such as including, without being limited to PC, PP, PVC, PET, bakelite and metallic substance to make at interior material.When selecting other base material except ABS, pre-treatment coating can carry out selection according to the performance of actual material and process requirements has pre-treatment coating or without pre-treatment coating.
As the etch state figure that Fig. 3 nickel plating parts sample that obtain to by the utility model embodiment obtains after 72h CASS tests, with the nickel plating parts sample etch state figure that (under equal experiment condition) obtains after 72h CASS tests that Fig. 2 is prior art, can intuitively arrive through contrast, the corrosion vacancy 21 that existing sample produces after there is a large amount of plating exfoliations and corrosion after the test, seriously have impact on the quality of product coating.Fig. 3 then can find out, then only there is the surface micropore 31 of some amount on surface in the nickel plating sample that the utility model obtains, then equally only there is less corrosion hole 32 in section display, be the coating structure that corrosion hole that surface micropore and sacrifice layer produce all does not have to destroy parts, do not affect the use of product and attractive in appearance.
Fig. 4 and Fig. 5 is then respectively the nickel plating parts sample of prior art and the sample surfaces etch state figure of the nickel plating parts sample of the utility model embodiment gained after fluorgypsum experiment (336h, 336h, 168h) (in figure, circle inside is divided into Experimental Area), can find out in figure, the nickel plating parts sample surfaces of prior art is all subject to corrosion in various degree, it is very slight that the sample that the utility model obtains then is corroded degree, substantially do not have variable color.As can be seen here, the nickel plating parts that unquestionable technical solutions of the utility model obtain have more excellent coating stability and erosion resistance, make nickel plating parts more durable, attractive in appearance.
As can be seen from Fig. 6 and Fig. 7 coating potential ph diagram ph then, in the utility model scheme, no matter low potential layer is simple layer or lamination layer structure, to be when being corroded with low potential nickel dam as sacrifice layer, when low potential nickel dam is the composite bed of high-sulfur nickel dam and tiny crack nickel dam, the height of the current potential of high-sulfur nickel dam and tiny crack nickel dam regulates with actual production technique, can be that high-sulfur nickel dam electromotive force is slightly high, also can be that tiny crack nickel dam electromotive force is slightly high.
As shown in Figure 8, mechanism when the nickel plating parts that the utility model scheme obtains are corroded is: for form electroless nickel layer 809 in ABS substrate 1 layer by layer in figure, bottoming nickel dam 808, copper plate 3, half light nickel dam 62, full light nickel or husky fourth nickel dam 61, low potential nickel dam 141 and micropore nickel dam 142, ornament layer 802, corrosive medium 801 disperses corrosion current and enters low potential nickel dam 141 (to reduce the area of actual participation corrosion in the microvoid structure of micropore nickel dam 142, there is less corroded area, form multiple independently hot spot, thus dispersion corrosion current, delay corrosion speed), after corrosion forms erosional surface 805, the copper plate 3 of high potential is run into after erosional surface 805 runs through low potential nickel dam 141, rear termination longitudinally corrosion is that lateral encroaching is until corrode whole low potential nickel dam 141, just can carry out next step corrosion, until coating structure is destroyed by entirety.
This place embodiment to the non-limit part of the technical scope mid point value that the utility model is claimed, equally all in the scope that the utility model is claimed.
Technique means disclosed in the utility model scheme is not limited only to the technique means disclosed in above-mentioned technique means, also comprises the technical scheme be made up of above technical characteristic arbitrary combination.It is more than embodiment of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications are also considered as protection domain of the present utility model.
Claims (8)
1. super anti-corrosion nickel plating-chromium parts, these super anti-corrosion nickel plating-chromium parts comprise:
Base material;
Pre-treatment coating, its deposition over the whole substrate, pre-treatment coating is formed with copper plate; With
Half light nickel dam, it is formed on copper plate; With
Full light nickel dam or husky fourth nickel dam, it is formed at half light nickel dam; With
Functional layer, it is formed on full light nickel dam or husky fourth nickel dam, and wherein functional layer comprises low potential nickel dam and is formed at the micropore nickel dam on low potential nickel dam; With
Ornament layer, it is formed on micropore nickel dam, and described ornament layer is the arbitrary of trivalent chromium coating or sexavalent chrome coating.
2. the super anti-corrosion nickel plating-chromium parts of one according to claim 1, it is characterized in that, the potential difference between described micropore nickel dam and low potential nickel dam is within the scope of 10-120mv.
3. the super anti-corrosion nickel plating-chromium parts of one according to claim 1 and 2, is characterized in that, described low potential nickel dam include one deck in high-sulfur nickel dam, tiny crack nickel dam or two-layer between composite deposite.
4. the super anti-corrosion nickel plating-chromium parts of one according to claim 1 and 2, it is characterized in that, the potential difference between described micropore nickel dam and low potential nickel dam is within the scope of 20-100mv.
5. the super anti-corrosion nickel plating-chromium parts of one according to claim 3, it is characterized in that, the potential difference between described micropore nickel dam and low potential nickel dam is within the scope of 20-100mv.
6. the super anti-corrosion nickel plating-chromium parts of one according to claim 3, is characterized in that, when low potential nickel dam adopts the composite deposite of tiny crack nickel dam and high-sulfur nickel dam, between tiny crack nickel dam and high-sulfur nickel dam, potential difference is in 10-80mv.
7. the super anti-corrosion nickel plating-chromium parts of one according to claim 1, is characterized in that, described full light nickel dam or the potential difference between husky fourth nickel dam and low potential nickel dam are within the scope of 0-100mv.
8. the super anti-corrosion nickel plating-chromium parts of one according to claim 1, is characterized in that, the potential difference between described half light nickel dam and full light nickel dam or husky fourth nickel dam is within the scope of 100-200mv.
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| CN104775143A (en) * | 2015-03-11 | 2015-07-15 | 嘉兴敏惠汽车零部件有限公司 | Multilayer ultra corrosion resistant nickel-chromium plating part and manufacturing method thereof |
| CN104775142A (en) * | 2015-03-11 | 2015-07-15 | 嘉兴敏惠汽车零部件有限公司 | Ultra-corrosion-resistant nickel-chromium plating component and manufacturing method thereof |
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| CN104775143A (en) * | 2015-03-11 | 2015-07-15 | 嘉兴敏惠汽车零部件有限公司 | Multilayer ultra corrosion resistant nickel-chromium plating part and manufacturing method thereof |
| CN104775142A (en) * | 2015-03-11 | 2015-07-15 | 嘉兴敏惠汽车零部件有限公司 | Ultra-corrosion-resistant nickel-chromium plating component and manufacturing method thereof |
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| CN104775142B (en) * | 2015-03-11 | 2020-08-18 | 嘉兴敏惠汽车零部件有限公司 | Super-corrosion-resistant nickel-chromium plated part and manufacturing method thereof |
| CN104775143B (en) * | 2015-03-11 | 2020-08-18 | 嘉兴敏惠汽车零部件有限公司 | Multilayer super corrosion resistant nickel-chromium plated component and method of making same |
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| CN106498480A (en) * | 2016-11-29 | 2017-03-15 | 延康汽车零部件如皋有限公司 | A kind of nickel seals handling process |
| CN108374186A (en) * | 2018-03-30 | 2018-08-07 | 芜湖强振汽车紧固件有限公司 | A kind of automobile-used fastener electro-plating method |
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