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CN111850623A - Electroplating solution and electroplating process for obtaining suede nickel layer - Google Patents

Electroplating solution and electroplating process for obtaining suede nickel layer Download PDF

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Publication number
CN111850623A
CN111850623A CN202010381878.XA CN202010381878A CN111850623A CN 111850623 A CN111850623 A CN 111850623A CN 202010381878 A CN202010381878 A CN 202010381878A CN 111850623 A CN111850623 A CN 111850623A
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electroplating
dimethyl benzyl
obtaining
nickel
chloride
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骆祖文
王鲁艳
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Dexin Chemical Shandong Co ltd
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/12Electroplating: Baths therefor from solutions of nickel or cobalt

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Abstract

The invention discloses an electroplating solution and an electroplating process for obtaining a suede nickel layer, and mainly relates to the field of metal decorative surface treatment. The electroplating solution comprises the following raw materials: 430-520 g/L of nickel sulfate; 30-50 g/L of nickel chloride; 30-50 g/L of boric acid; 2-5 g/L of saccharin sodium; 0.5-3 g/L of sodium allylsulfonate; 0.01-6 mg/L of polyethylene glycol type ionic surfactant; 0.5-10 mg/L of quaternary ammonium salt cationic surfactant, and the process comprises using the electroplating solution, wherein the treatment temperature is 48-55 ℃, the pH value is 3.9-4.5, and the cathode current density is 3.9-4.5A/dm2The stirring mode is cathode movement and cathode rotation, and the circulation filtration is not available. The invention has the beneficial effects that: different suede effects are obtained by adjusting the composition and content of the sanding agent, so that the requirements of different customers in the market on suede nickel are met.

Description

Electroplating solution and electroplating process for obtaining suede nickel layer
Technical Field
The invention relates to the field of metal decorative surface treatment, in particular to electroplating solution and an electroplating process for obtaining a suede nickel layer.
Background
The suede nickel is an important process in decorative surface treatment, has the characteristics of beautiful appearance, fine and soft color, low internal stress and good corrosion resistance, can be directly used as a protective decorative outer layer, and can also be coated with other metals such as chromium, gold, silver and the like to obtain more excellent protective decorative effects. At present, suede nickel is widely applied in the industries of automobile decoration, electronic products, daily hardware, cultural goods and the like.
The earliest textured nickel was produced by mechanical means, and the products obtained by this method were rough in surface, matt, and labor intensive, and were essentially eliminated. Currently, there are two general methods for obtaining textured nickel: a composite electrodeposition method and an emulsifier method. The composite electrodeposition method is that the dispersed phase comprising metal compound is added into the working liquid and suspended in the working liquid to form uneven nickel layer through co-deposition with nickel ion. The suede nickel surface formed by the technology has unsatisfactory glossiness, and the working solution is not easy to maintain and is limited in application. The emulsifier method is characterized in that a sanding emulsifier is introduced into the Watt nickel working solution, the sanding emulsifier generally consists of one or two nonionic surfactants, the nonionic surfactants have abnormal insolubility performance, the solubility of the nonionic surfactants is reduced along with the temperature rise, and when the temperature rises to a cloud point, the nonionic surfactants have association with water, ether bonds can be unhooked, and the solution is separated out to be turbid. When the diameter of the small liquid beads formed by precipitation reaches 5-30nm, the liquid beads are in a powered state, nickel ions do not deposit on the adsorbed small liquid beads during discharge deposition, and after the liquid beads are desorbed, tiny pits are formed at the original adsorption points, so that an uneven surface can be formed by repeating the steps. The synergistic effect of the nonionic surfactant and the cationic surfactant can obtain a more uniform and beautiful suede nickel layer. The micro surface of the suede nickel prepared by the method has countless overlapped pits, and shows a soft pearl effect on the macro scale.
The emulsifier method is generally adopted in the industry nowadays to obtain the required suede nickel. However, in the current commercial products, the sanding is unstable, and after 3-4 hours, the sand is disturbed, even black spots and bright spots appear on the surface, so that the stability of the matte effect cannot be realized, the activated carbon needs to be frequently added for filtration and adsorption, and then the adjustment is carried out again, so that the maintenance is extremely difficult, the stable and continuous production cannot be realized, the efficiency is low, the matte effect is single, and the appearance requirements of different customers on the matte nickel cannot be met. Therefore, the development of a long-acting matte nickel process which can obtain different matte effects by adjusting the composition of the working solution is urgently needed to meet the requirements of different customers.
Disclosure of Invention
The invention aims to provide an electroplating solution and an electroplating process for obtaining a nickel layer on a suede surface, which can obtain different suede surface effects by adjusting the composition and content of a sanding agent so as to meet the requirements of different customers on the nickel on the suede surface in the market.
In order to achieve the purpose, the invention is realized by the following technical scheme:
an electroplating solution for obtaining a textured nickel layer comprises the following raw materials:
Figure BDA0002482463710000021
preferably, the raw materials comprise:
Figure BDA0002482463710000022
Figure BDA0002482463710000031
further preferably, the raw materials comprise:
Figure BDA0002482463710000032
n- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride 9 mg/L.
The polyethylene glycol type ionic surfactant comprises one or more of polyethylene glycol, fatty alcohol polyoxyethylene ether, alkylphenol polyoxyethylene ether, fatty acid polyoxyethylene ether and fatty amine polyoxyethylene ether.
The polyethylene glycol type ionic surfactant is polyethylene glycol with the molecular weight of 5000-.
The quaternary ammonium salt cationic surfactant comprises dodecyl dimethyl benzyl ammonium chloride, dodecyl dimethyl benzyl ammonium bromide, tetradecyl dimethyl benzyl ammonium chloride, tetradecyl dimethyl benzyl ammonium bromide, hexadecyl dimethyl benzyl ammonium chloride, hexadecyl dimethyl benzyl ammonium bromide, octadecyl dimethyl benzyl ammonium chloride, octadecyl dimethyl benzyl ammonium bromide, dodecyl trimethyl ammonium chloride and dodecyl trimethyl ammonium bromide, tetradecyltrimethylammonium chloride, tetradecyltrimethylammonium bromide, hexadecyltrimethylammonium chloride, hexadecyltrimethylammonium bromide, octadecyltrimethylammonium chloride, octadecyltrimethylammonium bromide, hexadecylpyridinium chloride, (p-isooctylphenoxyethoxyethyl) (benzyl) (dimethyl) ammonium chloride, N- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride.
The quaternary ammonium salt cationic surfactant is dodecyl dimethyl benzyl ammonium chloride and N- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride.
As another aspect of the present invention, an electroplating process using the above-mentioned electroplating solution, wherein the treatment temperature of the process is 48 to 55 ℃, the pH value is 3.9 to 4.5, and the cathode current density is 3.9 to 4.5A/dm2The stirring mode is cathode movement and cathode rotation, and the circulation filtration is not available.
The treatment temperature of the process is 52 ℃, the pH value is 4.0, and the cathode current density is 4A/dm2
Compared with the prior art, the invention has the beneficial effects that:
nickel sulfate, nickel chloride and boric acid are added into the electroplating solution as basic components, wherein the nickel sulfate mainly provides nickel ions and conductive substances, the nickel chloride mainly promotes the dissolution of the anode, and the boric acid is added into the electroplating solution as a pH value buffering agent to stabilize the pH value of the working solution to 3.9-4.5.
Sodium saccharin and sodium allylsulfonate are used as additive components and added into the electroplating solution, wherein the sodium saccharin is mainly used as a softening agent to reduce the internal stress of nickel matte and improve the flexibility of the nickel matte, and the sodium allylsulfonate is used to ensure the nickel matte to be crystallized finely and to be more uniform and fine.
The polyethylene glycol type nonionic surfactant and the quaternary ammonium salt type cationic surfactant function as a sanding agent in the working fluid. The polyethylene glycol type nonionic surfactant and the quaternary ammonium salt type cationic surfactant with different molecular weights can be used independently to obtain the nickel layer with the required suede effect, and can also be used in a matched manner, the addition amount is adjusted to obtain the suede nickel layers with different appearance effects, and various production requirements are met.
Wherein, the polyethylene glycol type nonionic surfactant mainly has the function of enabling the nickel layer to obtain the round pit suede effect. The quaternary ammonium salt cationic surfactant has obvious sanding effect. The matte nickel process has the advantages that various matte nickel with different requirements can be prepared by selecting and compounding the polyethylene glycol type nonionic surfactant and the quaternary ammonium salt type cationic surfactant with different molecular weights and adjusting the composition and the proportion of the sanding agent, the process is simple to maintain, stable in color and luster, capable of continuously working for more than 15 days without any treatment, well meets production and application, and has great economic benefits.
Drawings
FIG. 1 is an electron micrograph of example 1 of the present invention.
FIG. 2 is an electron micrograph of example 2 of the present invention.
FIG. 3 is an electron micrograph of example 3 of the present invention.
FIG. 4 is an electron micrograph of example 4 of the present invention.
FIG. 5 is an electron micrograph of example 5 of the present invention.
FIG. 6 shows a test piece of the HULL cell of example 5 of the present invention.
FIG. 7 shows the thickness distribution of the nickel layer of the test piece of the HULL cell of example 5 of the present invention.
Detailed Description
The invention will be further illustrated with reference to the following specific examples. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention may be made by those skilled in the art after reading the teaching of the present invention, and these equivalents also fall within the scope of the present application.
The instruments, reagents, materials and the like used in the following examples are conventional instruments, reagents, materials and the like in the prior art and are commercially available in a normal manner unless otherwise specified. Unless otherwise specified, the experimental methods, detection methods, and the like described in the following examples are conventional experimental methods, detection methods, and the like in the prior art.
Example 1: electroplating solution and electroplating process for obtaining suede nickel layer
Taking 1L of the plating solution as an example, the plating solution comprises the following raw materials:
Nickel sulfate: 470 g/L;
nickel chloride: 40 g/L;
boric acid: 40 g/L;
sodium saccharin: 3.8 g/L;
sodium allyl sulfonate: 1.8 g/L;
0.05mg/L of polyethylene glycol 10000;
0.1mg/L of polyethylene glycol 15000;
cetyl trimethylammonium bromide: 1 mg/L.
The electroplating solution is used for nickel plating, and the technological parameters comprise:
treatment temperature: 52 ℃;
pH value: 4.0;
cathode current density: 4A/dm2
Stirring mode: moving and rotating the cathode;
and (3) a filtering mode: and (4) filtering in a non-circulating way.
Example 2: electroplating solution and electroplating process for obtaining suede nickel layer
Taking 1L of the plating solution as an example, the plating solution comprises the following raw materials:
nickel sulfate: 470 g/L;
nickel chloride: 40 g/L;
boric acid: 40 g/L;
sodium saccharin: 3.8 g/L;
sodium allyl sulfonate: 1.8 g/L;
0.15mg/L of lauryl alcohol polyoxyethylene ether 10;
1.5mg/L of polyethylene glycol 15000;
dodecyl dimethyl benzyl ammonium chloride: 3 mg/L.
The electroplating solution is used for nickel plating, and the technological parameters comprise:
treatment temperature: 52 ℃;
pH value: 4.0;
cathode current density: 4A/dm2
Stirring mode: moving and rotating the cathode;
and (3) a filtering mode: and (4) filtering in a non-circulating way.
Example 3: electroplating solution and electroplating process for obtaining suede nickel layer
Taking 1L of the plating solution as an example, the plating solution comprises the following raw materials:
nickel sulfate: 470 g/L;
nickel chloride: 40 g/L;
boric acid: 40 g/L;
sodium saccharin: 3.8 g/L;
sodium allyl sulfonate: 1.8 g/L;
dodecyl dimethyl benzyl ammonium chloride: 1 mg/L;
(p-isooctylphenoxyethoxyethyl) (benzyl) (dimethyl) ammonium chloride: 3 mg/L.
The electroplating solution is used for nickel plating, and the technological parameters comprise:
treatment temperature: 52 ℃;
pH value: 4.0;
cathode current density: 4A/dm2
Stirring mode: moving and rotating the cathode;
and (3) a filtering mode: and (4) filtering in a non-circulating way.
Example 4: electroplating solution and electroplating process for obtaining suede nickel layer
Taking 1L of the plating solution as an example, the plating solution comprises the following raw materials:
nickel sulfate: 470 g/L;
nickel chloride: 40 g/L;
boric acid: 40 g/L;
sodium saccharin: 3.8 g/L;
sodium allyl sulfonate: 1.8 g/L;
0.2g/L of nonylphenol polyoxyethylene ether 15;
(p-isooctylphenoxyethoxyethyl) (benzyl) (dimethyl) ammonium chloride: 3 mg/L;
dodecyl trimethyl ammonium bromide: 9 mg/L.
The electroplating solution is used for nickel plating, and the technological parameters comprise:
treatment temperature: 52 ℃;
pH value: 4.0;
cathode current density: 4A/dm2
Stirring mode: moving and rotating the cathode;
And (3) a filtering mode: and (4) filtering in a non-circulating way.
Example 5: electroplating solution and electroplating process for obtaining suede nickel layer
Taking 1L of the plating solution as an example, the plating solution comprises the following raw materials:
nickel sulfate: 470 g/L;
nickel chloride: 40 g/L;
boric acid: 40 g/L;
sodium saccharin: 3.8 g/L;
sodium allyl sulfonate: 1.8 g/L;
0.15mg/L of polyethylene glycol 10000;
1.5mg/L of polyethylene glycol 15000;
dodecyl dimethyl benzyl ammonium chloride: 3 mg/L;
n- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride: 9 mg/L.
The electroplating solution is used for nickel plating, and the technological parameters comprise:
treatment temperature: 52 ℃;
pH value: 4.0;
cathode current density: 4A/dm2
Stirring mode: moving and rotating the cathode;
and (3) a filtering mode: and (4) filtering in a non-circulating way.
Example 6: performance testing
The test pieces obtained by electroplating treatment using the electroplating solutions and processes described in examples 1 to 5 were tested as follows:
1. electron microscope detection SEM
The results of the square groove test conducted with reference to the process parameters of examples 1, 2, 3, 4 and 5 are shown in the following figures 1, 2, 3, 4 and 5, respectively, and the results of the SEM detection of the test pieces obtained by 300X and 500X times are shown in the figures.
As can be seen from FIGS. 1,2,3,4 and 5, different combinations of different contents of the sanding agent can make the surface of the nickel layer show different microscopic effects, and the surface has larger or smaller circular pits or is sparse or dense. By adjusting the composition and content of the sanding agent in the working solution, a nickel layer with a proper suede effect required by a customer can be obtained, and the customer requirements are met.
2. HULL cell experiment
Referring to the process of example 5, a HULL bath test was conducted and test pieces were subjected to an appearance test and a nickel layer thickness distribution test. The experimental results show that: from the high zone to the low zone, the test piece surface is fine and uniform, the appearance is soft, no bright spot or black spot exists, and the test piece effect is as shown in FIG. 6. The thickness distribution of the nickel layer is good, and the thickness of the nickel layer is reduced regularly along with the difference of current density, as shown in figure 7.
3. Test of Process stability
The combination of example 5 was compounded, and 10 test pieces of the continuous HULL cell were used to observe the change of nickel layer. The experimental results show that: the 10 th test piece has basically the same effect as the first suede, has no obvious difference, and has no bright spot and black spot on the nickel layer, and is uniform and fine.
The factory uses the embodiment 5 for production, does not need to carry out large treatment and readjust the working solution for more than 15 days, is stable and can carry out continuous production, improves the production efficiency and greatly reduces the cost.

Claims (9)

1. The electroplating solution for obtaining the matte nickel layer is characterized by comprising the following raw materials:
Figure FDA0002482463700000011
2. the electroplating bath for obtaining textured nickel layers as claimed in claim 1, wherein the raw materials comprise:
Figure FDA0002482463700000012
3. the electroplating bath for obtaining textured nickel layers as claimed in claim 1, wherein the raw materials comprise:
Figure FDA0002482463700000013
Figure FDA0002482463700000021
4. the electroplating solution for obtaining the textured nickel layer according to claim 1, wherein the polyethylene glycol type ionic surfactant comprises one or more of polyethylene glycol, fatty alcohol polyoxyethylene ether, alkylphenol polyoxyethylene ether, fatty acid polyoxyethylene ether and fatty amine polyoxyethylene ether.
5. The electroplating bath for obtaining Ni-textured layer as claimed in claim 4, wherein the PEG-type ionic surfactant is PEG with molecular weight of 5000-.
6. The electroplating bath for obtaining matte nickel layers according to claim 1, wherein the quaternary ammonium salt cationic surfactant comprises dodecyl dimethyl benzyl ammonium chloride, dodecyl dimethyl benzyl ammonium bromide, tetradecyl dimethyl benzyl ammonium chloride, tetradecyl dimethyl benzyl ammonium bromide, hexadecyl dimethyl benzyl ammonium chloride, hexadecyl dimethyl benzyl ammonium bromide, octadecyl dimethyl benzyl ammonium chloride, octadecyl dimethyl benzyl ammonium bromide, dodecyl trimethyl ammonium chloride, dodecyl trimethyl ammonium bromide, tetradecyl trimethyl ammonium chloride, tetradecyl trimethyl ammonium bromide, hexadecyl trimethyl ammonium chloride, hexadecyl trimethyl ammonium bromide, octadecyl trimethyl ammonium chloride, octadecyl trimethyl ammonium bromide, hexadecyl pyridine chloride, (p-isooctyl phenoxy ethoxy) (benzyl) (dimethyl) ammonium chloride, n-butyl dimethyl benzyl ammonium bromide, n-butyl dimethyl benzyl, One or more of N- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride.
7. The electroplating bath for obtaining textured nickel layers according to claim 6, wherein the quaternary ammonium salt cationic surfactants are dodecyl dimethyl benzyl ammonium chloride and N- { [ N- (2-lauroyloxyethyl) carbamoyl ] methyl } pyridinium chloride.
8. Electroplating process, characterized in that the electroplating solution for obtaining the textured nickel layer according to any one of claims 1 to 8 is used, and the process has a treatment temperature of 48 to 55 ℃, a pH value of 3.9 to 4.5 and a cathodic current density of 3.9 to 4.5A/dm2The stirring mode is cathode movement and cathode rotation, and the circulation filtration is not available.
9. An electroplating process according to claim 8, wherein the process is carried out at a temperature of 52 ℃, a pH of 4.0 and a cathodic current density of 4A/dm2
CN202010381878.XA 2020-05-08 2020-05-08 Electroplating solution and electroplating process for obtaining suede nickel layer Pending CN111850623A (en)

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