CN104364421B - Make the method for nonconductive plastic material surface metalation - Google Patents

Make the method for nonconductive plastic material surface metalation Download PDF

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CN104364421B
CN104364421B CN201380029727.6A CN201380029727A CN104364421B CN 104364421 B CN104364421 B CN 104364421B CN 201380029727 A CN201380029727 A CN 201380029727A CN 104364421 B CN104364421 B CN 104364421B
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solution
frosting
metal
chloranion
volume
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CN104364421A (en
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L.纳鲁斯克维丘斯
D.布迪洛夫斯基斯
O.吉利内
L.塔马索斯凯特塔马休奈特
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Atotech Deutschland GmbH and Co KG
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    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/2006Pretreatment of the material to be coated of organic surfaces, e.g. resins by other methods than those of C23C18/22 - C23C18/30
    • C23C18/2046Pretreatment of the material to be coated of organic surfaces, e.g. resins by other methods than those of C23C18/22 - C23C18/30 by chemical pretreatment
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    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/1601Process or apparatus
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    • C23C18/1651Two or more layers only obtained by electroless plating
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    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/2006Pretreatment of the material to be coated of organic surfaces, e.g. resins by other methods than those of C23C18/22 - C23C18/30
    • C23C18/2046Pretreatment of the material to be coated of organic surfaces, e.g. resins by other methods than those of C23C18/22 - C23C18/30 by chemical pretreatment
    • C23C18/2073Multistep pretreatment
    • C23C18/2086Multistep pretreatment with use of organic or inorganic compounds other than metals, first
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/22Roughening, e.g. by etching
    • C23C18/24Roughening, e.g. by etching using acid aqueous solutions
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/28Sensitising or activating
    • C23C18/285Sensitising or activating with tin based compound or composition
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/28Sensitising or activating
    • C23C18/30Activating or accelerating or sensitising with palladium or other noble metal
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/32Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents
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    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/32Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents
    • C23C18/36Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents using hypophosphites
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/38Coating with copper
    • C23C18/40Coating with copper using reducing agents
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    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/38Coating with copper
    • C23C18/40Coating with copper using reducing agents
    • C23C18/405Formaldehyde

Abstract

The present invention relates to make the method that nonconductive plastic material metallizes with not chromyl etching solution.Etching solution is based on the sulfuric acid solution for including chloranion source.After plastics are handled with etching solution, made by known method plastics metalizing.

Description

Make the method for nonconductive plastic material surface metalation
Invention field
The present invention relates to the pretreatment nonconductive plastic material surface before metallization, and it can be applied to wherein need plastic section The dicoration of part or the difference industry of functional metal coating.Pretreatment is carried out in not chromyl solution.
Background of invention
The conventional method on pretreatment nonconductive plastic material surface before electroless metallising (mainly electroless nickel plating or copper facing) Consist of:Surface is etched in chromyl solution, is then activated in the ion or colloidal solution of palladium compound, and And reduced in sodium hypophosphite solution (in most cases) or in acid solution (the usual salt of palladium ion or colloid palladium particle Acid) middle acceleration (adsorbing respectively on frosting).
For hydrophiling, it is necessary to etch non-conductive matrix surface during pre-treatment step so that surface method its Its stage becomes hydrophilic in aqueous, while adsorbing the palladium salt of sufficient amount, and ensures coat of metal appropriate combination to non-conductive Frosting.In order to trigger metal electroless deposition on plastics, activated, then reduction or acceleration.Then, by urging automatically Change reaction progress metal electroless in metallization solution, wherein the metal deposited on the surface is as further depositing Catalyst.This electroless mainly uses metallic nickel and copper.
Then, it can be electrolysed on the first metal layer or electrochemical plating.Can apply various metals, for example chromium, nickel, copper and Other alloys of brass or aforementioned metal.
The major defect of conventional method is related to the carcinogenicity of chromic acid in etching solution.In addition, during electroless deposition step The part of the metal of deposition, such as nickel, the also support that covering plastisol insulate, this causes in subsequent electrochemical metal plating Solution metal loss, it is therefore undesirable.
The various methods for overcoming this problem are had pointed out in the prior art.
The A1 of U.S. Patent Application No. 2005/0199587, which is disclosed, a kind of is including the acid solution of 20-70g/l potassium permanganate The method on middle etching nonconductive plastic material surface.Optimal KMnO in solution mentioned above4Concentration is close to 50g/l.It is less than in concentration During 20g/l, solution is invalid, and upper limit of concentration is determined by the solubility of potassium permanganate.After etching, in the palladium salt solution comprising amine Activation, and the further reduction treatment for example in boron hydride, hypophosphites or hydrazine solution.
However, the method has significant drawback.In the etch solution (it is recommended that about 50g/l, is carried under high permanganate concentration 48% volume phosphoric acid), it is decomposed quickly, especially in high temperature.It is recommended that temperature is 100 ℉, i.e., 37 DEG C.Experiment is it has been shown that warm herein Degree, solution became invalid after 4 to 6 hours, i.e. frosting not hydrophiling, and some places are kept during metallizing It is not plated, the adhesive force with plastics in plating zones is very weak.Need to adjust solution through conventional new peak manganate part, it is high Manganate is not cheap.In addition, also generating insoluble permanganate catabolite, the surface metallized is polluted.
In addition, when being manganese dioxide with etch reaction products plating, the etching in permanganate solution makes support Plastisol insulator surface is activated.The latter promotes palladium compound to be adsorbed on plastisol, and this tends to heavy in electroless metal Product GOLD FROM PLATING SOLUTION categoryization.Generation manganese dioxide is the feature of the permanganate etch solution of any composition on the surface.Therefore, originally The critically important purpose of invention is to avoid backbone metal, and avoids the metal loss in subsequent metalization level.
Lithuania number of patent application LT 2008-082 are directed to before metallization pre-process nonconductive plastic material surface.Its Disclosed in a kind of pretreatment compositions, using 10-80 DEG C of temperature, in 13mol/L (about 75% volume) -17mol/L (about 90% bodies Product) concentration sulfuric acid in 0,005-0,2M oxidizing agent solutions etch such as polyimides 1-2 minutes, wherein oxidant can be KMnO4、HClO4、V2O5、KClO3.In chlorate anions (ClO3 -, M=83.5g/mol) in the case of, this is equivalent to 0.4-16.7g/l Concentration.
An example is provided in the table 2 applied at this, example includes 7mol/L (about 50% volume) sulfuric acid and 0.2mol/L (16.7g/L) chlorate anions.However, having shown the chlorate anions of such high concentration causes preprocessing solution fast decoupled, this, which does not conform to, needs Will.
Invention description
Therefore, the present invention is based on problems with:So far also fail to be realized with Environmental security mode and be made up of nonconductive plastic material Product metallization, and the metal level adhesive strength for having enough reliability of technology and then applying is enough.
It is therefore an object of the present invention to the etching solution on the nonconductive plastic material surface for pre-treatment preparations is found, these It is nontoxic, but enough adhesive strengths is provided for the metal level applied on frosting.
This purpose is achieved by the following way:Using in the application can comprising 0.2 to 15.0g/l in 50-80% volume sulfuric acid Molten chlorate (is based on KClO3, M=122.55, i.e. 0.0016mol/l to 0.12mol/l) etching solution etching frosting make For the processing method of the frosting before electroless metallising, processing method is consisted of:With the inorganic acid with oxidant Solution etches plastics, is activated by palladium salt solution, and by reducing or accelerating solution to handle.Etching is preferably in room temperature (15-28 DEG C, preferably 20-25 DEG C) carry out, but also can up to 40 DEG C or 50 DEG C higher temperature carry out, condition be solution stability by Control.Preprocessing solution can optionally include up to 20g/l another oxidant, and it has the standard oxidation electricity more than chlorate anions Position.
Etching period can be determined with matrix material and its alteration of form by routine test.It is general 1 and 20 minute it Between, preferably no longer than 10 minutes.
Chloranion source can be any water soluble salt.Most-often used sodium chlorate and potassium chlorate.
In etching solution the concentration of chloranion be 0.0016mol/l to 0.12mol/l, or preferably of up to 0.03mol/ L is even more preferably up to 0.04mol/l.It is preferred that scope between 0.003mol/l and 0.08mol/l, or in 0.01mol/ Between l and 0.06mol/l or between 0.004mol/l and 0.04mol/l.
The concentration of sulfuric acid is even more excellent preferably between 55% volume and 70% volume between 50% volume and 80% volume It is selected between 60% volume and 65% volume.
Optionally other acid can be used as comprising phosphoric acid in the etch solution.The concentration of phosphoric acid is generally 10% volume to 40% body Product, preferably between 15% volume and 25% volume or 30% volume.When in addition using phosphoric acid, plating can be unexpectedly improved in addition The adhesive force of metal level.
The mixture of phosphoric acid is particularly preferred between sulfuric acid and 20% volume and 30% volume between 60% volume and 65% volume.
The method on pretreated plastic surface includes before electroless metallising, is lost in the inorganic acid solution added with oxidant Plastics are carved, are activated in palladium salt solution, and are handled in reducing or accelerating solution, it is characterised in that pass through 50-80% bodies in room temperature The solution etching plastic table of 0.02-15.0g/l soluble chlorines hydrochlorate (for example, 0.5-5g/l soluble chlorines hydrochlorate) in product sulfuric acid Face, and handled in addition in alkali hydroxide soln, then activated and molten with reduction/acceleration by palladium compound solution Liquid processing.
Etching solution can optionally include 2 to 20g/l another oxidant, and it has the standard oxygen more than chloranion Change current potential.
Alkali metal chlorate and sulfuric acid generation yellow compound, it is in H2SO4Standard oxidizing potential in solution medium is enough Reacted in room temperature and frosting.Due to this reaction, frosting becomes hydrophilic, and adsorbs palladium compound with sufficient intensity. Yellow reaction product between chlorate and sulfuric acid is the poisonous substance of palladium catalyst.During etching, the plasticising that it penetrates support is molten Glue insulator surface layer, and prevention electroless deposition of metals on plastisol in electroless metallising solution, in nonconductive plastic material The metallization processes occurred on surface are unaffected.
In 1 to 2g/l sodium chlorate or potassium chlorate and 5 to 10g/l second strong oxidizer (such as NaBiO3) dissolving when, etching Property is kept for a couple of days in room temperature, and solution can be used in the case where not adjusting.If only including sodium chlorate/potassium chlorate in the solution, erosion Carve the time (most long 24 hours) that property keeps much shorter.
Make its important difference for being different from the proposed method of permanganate etch be characterized in coating and plastics it Between obtain very high adhesion value, usually more than 1.2 to 1.3kg/cm.Except the composition and etching period of etching solution are (to each Composition has the optimal etch time) outside, these values additionally depend on the composition of activated solution.Generally, when using actual activated solution, Obtained adhesion value is higher than those values obtained with colloidal activating solution.
It can be prepared as follows etching solution:
The 700ml concentrated sulfuric acids are made to be mixed with 300ml deionized waters.Cool down solution.Then 2g potassium chlorate and 10g perchloric acid are made Sodium is dissolved in solution.Solution is ready to use.It is optional to be better than the second oxidant sodium perchlorate of potassium chloride.It increases composition Useful life, but need not it obtain the well attached of subsequent metal plating layer.
When the amount for preparing water used in solution is compared with sulfuric acid more than 50% volume, chloranion and sulfuric acid molecule it Between do not generate yellow plastic oxidized compound, therefore, 50% volume is preferably not to be exceeded in the water content of solution.
When the amount for preparing water used in solution is compared with sulfuric acid less than 20% volume, because sulfuric acid concentration is too high, in the etching phase Between frosting decompose, therefore, there is no adhesive force between chemical nickel coating and plastics.
If the amount for being dissolved in the potassium chlorate of solution is less than 0.5g/l, etching process is time-consuming to be longer than 15 minutes, therefore, this dense Degree is unacceptable.
It is considerable after minimum etching period (i.e. 2 to 3 minutes) if being dissolved in the amount of the potassium chlorate of solution more than 5.0g/l Over etching is observed, this produces the adhesive strength of much weaker, and therefore, this high concentration cl hydrochlorate is also unacceptable.However, according to Matrix material, the higher concentration for producing the highest 15g/l of enough adhesive force is also subjected to.
The purpose of the present invention is further realized by the following methods of the present invention:
Make the method for the nonconductive plastic material surface metalation of product, methods described includes following methods step:
A frosting) is etched with the above-mentioned etching solution comprising chloranion source, the chloranion source is obtained 0.0016 to 0.12mol/l chloranion concentration in 50-80% volume sulfuric acid;
B) with the solution processing frosting of metallic colloid or metallic compound, the metal is selected from periodic table of elements I The metal of transition group and periodic table of elements VIII transition groups;And
C) metallization of plastic surface is made with metallization solution;
It will be appreciated that in the context of the present invention, product refers to be made up or with least one of at least one nonconductive plastic material Plant the product of at least one layer of covering in nonconductive plastic material.Therefore, product has the surface of at least one nonconductive plastic material.Ying Liao Solution, in the context of the present invention, frosting means these described surfaces of product.
The method and step of the present invention, but need not be with immediately order to provide that order is carried out.Other method and steps can be carried out, and And cleaning step can be additionally carried out in all cases between the steps, preferably use water.
Frosting is made up of at least one nonconductive plastic material.In one embodiment of the invention, it is at least one Nonconductive plastic material be selected from acrylonitrile-butadiene-styrene copolymer (Acrylonitrile Butadiene-Styrene copolymer), polyamide (PA), makrolon (PC), With Acrylonitrile Butadiene-Styrene copolymer and the mixture of at least one other polymer.
In a preferred embodiment of the invention, nonconductive plastic material is Acrylonitrile Butadiene-Styrene copolymer or Acrylonitrile Butadiene-Styrene copolymer and at least one Plant the mixture of other polymer.At least one other polymer is more preferably makrolon (PC), and this represents particularly preferred ABS/PC mixtures.
Etching solution of the present invention is preferably free of any chromium or chromium compound, and etching solution is both free of chromium (III) ion, also not Containing chromium (VI) ion.Therefore, etching solution of the present invention is free of chromium or chromium compound, and etching solution is free of chromium (III) ion and chromium (VI) ion.
In another preferred embodiment of the present invention, in method and step A) and B) between carry out method additionally below Step:
A i) frosting is handled in the solution including alkaline solution.
Other method and step A i) it is also referred to as neutralisation treatment.Any alkaline source, the aqueous solution of sodium hydroxide can be used It is preferred.
The present invention another for selecting embodiment in, in method and step A) and B) between carry out method additionally below Step:
A i) handle plastic table in comprising the solution for chloranion and the reducing agent of the second optional oxidant Face.
Other method and step A i) it is also referred to as reduction treatment.This reduction treatment reduces the chlorine for being attached to frosting Acid ion and the second optional oxidant, and promote to remove these ions.Reducing agent is selected from hydroxylammonium sulfate, hydroxylammonium chloride And hydrogen peroxide.
The method of the present invention further comprises method and step B), wherein frosting metallic colloid or metallic compound Solution processing.
The metal of metallic colloid or metallic compound is selected from the periodic table of elements (PTE) I transition groups and PTE VIII transition The metal of race.
The metal of PTE VIII transition groups is selected from the mixture of palladium, platinum, iridium, rhodium and two or more these metals. The metal of PTE I transition groups is selected from gold, silver and the mixture of these metals.
Preferred metal in metallic colloid is palladium.Metallic colloid protective colloid-stabilisedization.Protective colloid is selected from gold Belong to protective colloid, organic protective colloid and other protective colloids.It is preferred that being used as metal coating colloid with tin ion.Have Machine protective colloid is selected from polyvinyl alcohol, polyvinylpyrrolidone and gelatin, preferably polyvinyl alcohol.
In a preferred embodiment of the invention, method and step B) in metallic colloid solution be with palladium/tin glue The activator solution of body.This colloidal solution is obtained from palladium salt, tin (II) salt and inorganic acid.It is preferred that palladium salt be palladium bichloride.It is excellent Tin (II) salt of choosing is stannic chloride (II).Inorganic acid can be made up of hydrochloric acid or sulfuric acid, preferably hydrochloric acid.Colloidal solution by by Stannic chloride (II) makes palladium bichloride be reduced into palladium to generate.It is complete that palladium bichloride, which changes into colloid, and therefore, colloidal solution no longer contains Any palladium bichloride.The concentration of palladium is based on Pd2+For 5mg/l-100mg/l, more preferably preferably 20mg/l-50mg/l, 30mg/l- 45mg/l.The concentration of stannic chloride (II) is based on Sn2+For 0.5g/l-10g/l, more preferably preferably 1g/l-5g/l, 2g/l-4g/l.Salt The concentration of acid is 100ml/l -300ml/l (37% weight HCl).In addition, palladium/tin colloid solution also includes tin (IV) ion, tin (IV) ion is generated by tin (II) ionic oxide formation.In method and step B) during colloidal solution temperature be 20 DEG C -50 DEG C, preferably 35℃-45℃.It is 0.5min-10min, more preferably preferably 2min-5min, 3min- using the processing time of activator solution 5min。
In another embodiment of the present invention, in method and step B) in, replace metal with the solution of metallic compound Colloid.The solution of metallic compound used is the solution comprising acid and metal salt.Metal in metal salt by one or more with Upper listed PTE I and VIII transition groups metal composition.Metal salt can be palladium salt, preferably palladium bichloride, palladium sulfate or acetic acid Palladium, or silver salt, preferably silver acetate.Acid is preferably hydrochloric acid.Or, it is possible to use metal complex, such as palladium complex salt, for example Palladium-aminopyridine complex salts.Method and step B) in metallic compound deposited with the concentration based on metal 40mg/l to 80mg/l .The solution of metallic compound can be used in 25 DEG C to 70 DEG C temperature, preferably at 25 DEG C.Utilize the processing of metal compound solution Time is 0.5min -10min, more preferably preferably 2min -6min, 3min -5min.
In method and step A) and B) between can carry out method and step additionally below:
A ii) frosting is handled in acidic aqueous solution.
It is preferred that in method and step A i) and B) between carry out method and step A ii).In the method for the invention, if in side Method step A i) protective cradle afterwards, then more preferably in protective cradle and method and step B) between carry out method and step A ii).
In method and step A ii) in processing frosting be also referred to as preceding dipping, acidic aqueous solution is used as preceding dipping solution.Before Dipping solution have and method and step B) in colloidal solution identical constitute, but in colloid and its protective colloid be not present gold Category.In method and step B) it is middle using in the case of palladium/tin colloid solution, if colloidal solution equally includes hydrochloric acid, preceding dipping Solution exclusively includes hydrochloric acid.For preceding dipping, dipping solution is just enough before environment temperature briefly immerses.Do not clean plastics Surface, in preceding dipping solution handle after, they are further directly used into method and step B) colloidal solution handle.
In method and step B) when including handling frosting with colloidal metal solution, preferably carry out method and step A ii). Can be in method and step B) include carrying out method and step A ii when handling frosting with metal compound solution).
In method and step B) after middle metallic colloid or metallic compound processing frosting, it can be cleaned.
In another embodiment of the present invention, in method and step B) and C) between carry out additionally below method step Suddenly:
B i) frosting is handled in acidic aqueous solution, and
B ii) make frosting electroless metallising in metallization solution.
Embodiment is shown schematically in table 1.
Method and step Composition Time Temperature
A) etch Table 2 4-6min 22℃
A i) neutralize 10g/l NaOH 4min 20℃
A ii) preceding dipping Hydrochloric acid, about 10% weight 1min 20℃
B) activate Palladium/tin colloid in hydrochloric acid solution 3-6min 20-45℃
B i) accelerate Sulfuric acid (5%) 2-6min 40-50℃
B ii) electroless metal deposition Electronation nickel plating or copper facing 6-20min 30-50℃
C) metal deposit For example, Cu electroplating or nickel plating 15-70min 20-35℃
Table 1:Plastics metalizing embodiment
When product will be metallized by electroless metallising method, i.e., the first metal layer will be by being applied to modeling without method for electrically When expecting surface, these other method and step B i are utilized) and B ii).
If method and step B) in activation carried out with metallic colloid, in order to from frosting remove colloidal solution in Colloid composition such as protective colloid, in method and step B i) in accelerator solution handle frosting.If in method Step B) in colloid in colloidal solution be palladium/tin colloid, then accelerator solution preferably used for acid the aqueous solution.For example, sour Selected from sulfuric acid, hydrochloric acid, citric acid and tetrafluoro boric acid.In the case of palladium/tin colloid, accelerator solution helps to remove as protection The tin compound of property colloid.
Or, in method and step B) in replace metallic colloid to be used for when activating with the solution of metallic compound, in method Step B i) middle progress reducing agent processing.Then, if the solution of metallic compound is the hydrochloric acid solution or silver salt of palladium bichloride During acid solution, the reductant solution used for this purpose includes hydrochloric acid and stannic chloride (II).Reductant solution also can be comprising another A kind of reducing agent, such as NaH2PO2Or borine or boron hydride, such as alkali metal borine or alkaline-earth metal borine or dimethylamino Base borine.It is preferred that using NaH in reductant solution2PO2
In method and step B i) in reductant solution accelerate or handle after, frosting can be cleaned first.
In method and step B i) and optional one or more cleaning steps after, carry out method and step B ii), wherein making modeling Expect surface electroless metallising.For example, completing electroless nickel plating with conventional nickel bath, the nickel bath especially includes nickel sulfate, is used as reduction The hypophosphites (for example, sodium hypophosphite) and organic complexing agent and pH adjusting agent (for example, buffer) of agent.Reducing agent used can be same Sample is the mixture of dimethyl amino borane or hypophosphites and dimethyl amino borane.
Or, electroless copper can be carried out with electroless copper bath, electroless copper bath generally comprises mantoquita, for example, copper sulphate or secondary phosphorus Sour copper;And reducing agent, such as formaldehyde or hypophosphites (such as alkali metal or ammonium salt) or hypophosphorous acid;And it is another or a variety of Complexing agent, such as tartaric acid;And pH adjusting agent, such as sodium hydroxide.
Then, in order to obtain feature or decorative surface, the surface electrolyzing gold that electric conductivity is so provided can further be made Categoryization.
The step C of the method for the present invention) it is to make metallization of plastic surface with metallization solution.Method and step C) in metal Change can be electrolysed progress.For electrolytic metal chemical, can with any required metal deposit bath for example deposition nickel, copper, silver, gold, tin, Zinc, iron, lead or their alloy.These deposition baths are familiar with by those skilled in the art.The bath of Watts nickel is typically used as bright nickel Bath, this bath includes nickel sulfate, nickel chloride and boric acid, is also used as additive comprising saccharin.The reality for the composition bathed as bright copper Example includes copper sulphate, sulfuric acid, sodium chloride and organosulfur compound, and wherein sulphur is in low-oxidation-state, such as organic sulfur compound or two Sulfide, is used as additive.
Method and step C) in the effect of metallization of plastic surface be frosting metal deposition, metal, which is selected from, to be used to deposit The metal listed above of bath.
In another embodiment of the present invention, in method and step C) method and step additionally below is carried out afterwards:
C i) metallized frosting is stored at elevated temperatures.
As wherein with metal by the idioelectric all electro-plating methods of wet chemical method plating, metal level is being applied Afterwards, the adhesive strength between metal and plastic substrate increases in the first stage.In room temperature, this process was completed after about 3 days.This can Substantially speeded up by storing at elevated temperatures.This process is completed after about 1 hour at 80 DEG C.It is assumed that initial low adhesive strength The thin water layer for forming electrostatic force by the interface between metal and non-conductive matrix and prevention is produced.
Therefore, method of the invention can apply the splendid adhesive strength of metal level with good process reliability and then Realize the nonconductive plastic material surface metalation of product.The adhesive strength for being administered to the metal level of frosting reaches up to 2.7N/ Mm (being approximately equivalent to 2.7kg/cm, 1kg/cm=0.98N/mm) or higher value.Therefore, the adhesive strength reached is also far above The intensity reached after frosting (see embodiment 2 and 3) can be etched according to prior art chromatosulfuric acid.
In general, commercial Application needs the adhesion value more than 0.8N/mm, and the thing for wanting plating non-complex to be molded Body.In general, the adhesive force of deposit is higher, and stability is better.
In addition, not only flat frosting is metallized by the method for the present invention with high-adhesion, and uneven shaping Frosting, such as spray head, also are provided with uniform strong adhesion metal coating.
Frosting is handled preferably in conventional impregnation methods by the method for the present invention, by by product successively wherein Solution is immersed in the container handled respectively to carry out.In the case, support can be secured the article to or be contained in drum To immerse solution.It is preferred fixed to support.Or, for example, by being placed on disk, and it is logical with horizontal direction continuous conveying Cross equipment, also can in so-called conveying equipment treatment articles.
Effective embodiment
Effective embodiment as described below is intended to explain the present invention.
Embodiment 1
According to the A1 of U.S. Patent Application No. 2005/0199587,50g/l KMnO are being included445% volume phosphoric acid solution In 37 DEG C in 5min (for ABS) or 15min (for PC/ABS) during, or with 0.5 to 5.0g/l KClO3And add Have in 50 to 80% volume sulfuric acid solutions of oxidant at 20 DEG C during 1 to 12min, etch ABS (acrylonitrile-butadienes-benzene Ethylene copolymer) and PC/ABS (mixture of 45% makrolon and 55% acrylonitrile-butadiene-styrene copolymer).Etching Afterwards, plastics are submerged to 1 to 2min, then in the true solution of palladium compound in the room temperature comprising 10g/l NaOH and in solution (colloidal solution is special for DOW Chemical Company's (" DOW ") for (5min, 20 DEG C) or colloidal solution (2min, 35 DEG C) Solution) middle activation.PdCl in true solution2Concentration is 0.1g/l, and pH value of solution is 2.7.After being activated in true Pd solution, make plastics In the solution of pH 9 comprising 20g/l sodium hypophosphites 5min is kept at 60 DEG C.After being activated in special colloidal solution, DOW is utilized Special acceleration solution handles plastics 2min at 40 DEG C.Then, plastics nickel plating is made with DOW Niposit-PM nickel plating process.Coating Quality is according to many factors evaluation, such as the plastisol of the frosting of complete or incomplete plating, plating or non-plating is exhausted The adhesive strength of edge support and electroless nickel and plastics.In order to evaluate adhesive force, thicken Ni coating in the bath of electrochemical copper, and measure Intensity (kg/cm) needed for peeling off the wide bars of 1cm from plastics.For ABS test specimens, the etching period in permanganate solution is 5min, is 15min to PC/ABS test specimens.For all test specimens, the etching period in solution of chlorate is 5min.For metal The plastics pretreatment condition of change and the result of metallization (electroless nickel plating) are shown down in table 2 below.
Table 2
* (remaining is activated in ion activation solution) is activated in special DOW colloidal solution.
Test specimen 1 to 4 shows that in the case of based on permanganate etch, the plastisol insulator of support is by electroless nickel Part plating, and in the case where being etched based on chlorate, insulator keeps clean.In addition, for ion and colloidal activating In the case of the chlorate etching of both solution, the adhesion value between Ni coating and ABS is significantly higher.
Identical result is observed in the case of PC/ABS (test specimen 5 to 8) electroless nickel plating:In chlorate engraving method, Plastisol insulator not plating, and adhesion value is significantly higher, especially when using ion activation solution.
As the KClO in etching solution3When concentration is less than 0.5g/l, ABS is not by plated with electroless nickel, or not exclusively plating (test specimen 9).In KClO3When concentration is more than 5g/l (test specimen 10), the over etching after etching 5min, therefore, coating adhesion value Significantly lower (being not enough to be used for practical application).In the KClO more than suggestion3During concentration value, class also is obtained to PC/ABS metallization Like result (test specimen 11 and 12).
H in the etch solution2SO4In the case that concentration is less than 50% volume, etchant is not effective enough, therefore, plastics root This is not by plated with electroless nickel, or not exclusively plating (test specimen 13).In H2SO4When concentration is higher than 80% volume (test specimen 14), occur Adhesive force between plastics over etching, and chemical nickel coating and plastics is not enough.
Embodiment 2
ABS plastic (Novodur P2MC, purchased from Ineos) circular base disk with 7cm diameters is fixed to stainless steel On silk.Then, as provided in table 4, matrix is undergone 4 minutes in the different pretreatments etching solution that 22 DEG C of temperature immerse the present invention (method order is shown in table 3).Then, underwater cleaning matrix is being flowed about 1 minute.In subsequent cleaning, neutralize (method and step A I) hydrochloric acid solutions of 300ml/l 36% (method and step A ii)) and are briefly immersed) after, based on palladium colloid (Adhemax Aktivator NA, purchased from Atotech, 100ppm palladiums) colloidal activating dose in 40 DEG C of activated matrix, 3 minutes (method and steps B))。
After subsequent cleaning, palladium removing particle containment vessel being removed at 40 DEG C 3 minutes, (Adhemax ACC1 accelerators, are purchased from Atotech, method and step B i)).Then make matrix at 45 DEG C (Adhemax LFS, are obtained within 10 minutes without nickel plating under foreign current From Atotech, method and step B ii)), cleaning, and in room temperature in 3.5A/dm2(Cupracid HT, are derived within 70 minutes for copper facing Atotech, method and step C)).After cleaning, by plate in 70 DEG C of storages 60 minutes (method and step C i)).Then, width is cut out with knife The plastic substrate bar of about 1cm metallization is spent, metal level is pulled away from plastics (ASTM B with Tensile Tester (being purchased from Instron) 533 1985,2009 again through).Obtain adhesive strength as shown in table 4.
Table 3:The order of method and step in embodiment 2
Table 4:According to the adhesive strength of the copper/nickel dam on different ABS mixtures of embodiment 2
From table 4 it became apparent that, by combining careful selection perchlorate concentration with sulfuric acid, can obtain very high attached Force value.Test specimen 1 shows, the low concentration (ClO equivalent to 0.0016mol/l as 0.2g/l potassium chlorate3 -Concentration) foot To obtain excellent adhesive force.Maximum is obtained in about 1.5g/l potassium chlorate scopes.Then, observable adhesive strength declines.Should It is noted that being compared with being etched in the solution for only including sulfuric acid, composition (table 4, test specimen 9 comprising sulfuric acid and phosphate mixture To 16) generally showing higher adhesion value in identical chloranion concentration, therefore particularly preferably.

Claims (14)

1. making the method for the nonconductive plastic material surface metalation of product, it the described method comprises the following steps:
A) frosting is etched with aqueous etching solution;
B the frosting) is handled with the solution of metallic colloid or metallic compound, the metal is selected from periodic table of elements I Group 4 transition metal and periodic table of elements group VIII transition metal;And
C) metallization of plastic surface is made with metallization solution;
It is characterized in that the etching solution, which is included, obtains 0.01 to the chloranion source of 0.08mol/L chloranion concentration With 50-80% volume sulfuric acid, wherein the etching solution be free of chromium III ions and chromium VI ions.
2. the method for claim 1, it is characterised in that in method and step A) in chloranion source in etching solution be selected from chlorine Sour sodium and potassium chlorate.
3. the method for claim 1, it is characterised in that chloranion concentration is 0.01mol/L-0.06mol/L.
4. the method for claim 1, it is characterised in that chloranion concentration is 0.01mol/L-0.04mol/L.
5. the method for claim 1, it is characterised in that sulfate ion concentration is the volume of 60% volume -70%.
6. the method for claim 1, it is characterised in that second oxidation of the etching solution further comprising 2 to 20g/L amount Agent, second oxidant has the standard oxidizing potential more than chloranion.
7. the method for claim 1, it is characterised in that the etching solution further includes phosphoric acid.
8. the method for claim 7, it is characterised in that phosphoric acid concentration is the volume of 10% volume -30%.
9. the method for claim 1, it is characterised in that method and step B) in metal be palladium.
10. the method for claim 1, it is characterised in that the frosting is made up of at least one nonconductive plastic material, and institute State at least one nonconductive plastic material and be selected from acrylonitrile-butadiene-styrene copolymer, polyamide, makrolon and acrylic nitrile-butadiene The mixture of diene-styrene copolymer and at least one other polymer.
11. the method for claim 1, it is characterised in that in method and step A) and B) between carry out method and step additionally below:
A i) frosting is handled in comprising the solution for the reducing agent of chloranion.
12. the method for claim 11, it is characterised in that the reducing agent is selected from hydroxylammonium sulfate, hydroxylammonium chloride and hydrogen peroxide.
13. the method for claim 1, it is characterised in that in method and step A) and B) between carry out method and step additionally below:
A i) frosting is handled in the solution containing the nertralizer comprising hydroxyl ion source.
14. the method for any one of preceding claims, it is characterised in that in method and step B) and C) between carry out additionally below Method and step:
B i) frosting is handled in acidic aqueous solution, and
B ii) make the frosting electroless metallising in metallization solution.
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LT6070B (en) 2012-12-07 2014-09-25 Atotech Deutschland Gmbh Preparation of plastic surface for chemical metallization process
US10920321B2 (en) 2014-05-30 2021-02-16 Uab Rekin International Chrome-free adhesion pre-treatment for plastics
US9506150B2 (en) 2014-10-13 2016-11-29 Rohm And Haas Electronic Materials Llc Metallization inhibitors for plastisol coated plating tools
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US20200087791A1 (en) * 2017-06-01 2020-03-19 Jcu Corporation Multi-stage resin surface etching method, and plating method on resin using same
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919768A (en) * 1989-09-22 1990-04-24 Shipley Company Inc. Electroplating process
US5160600A (en) * 1990-03-05 1992-11-03 Patel Gordhanbai N Chromic acid free etching of polymers for electroless plating
CN1508287A (en) * 2002-12-18 2004-06-30 Method for activating substrate for plating on plastic
LT2008082A (en) * 2008-10-28 2010-05-25 Chemijos Institutas Process for etching polyimide and other plastics
CN102409320A (en) * 2011-11-29 2012-04-11 沈阳工业大学 Electroplating pretreatment method for acrylonitrile butadiene styrene (ABS) plastic surface

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52112668A (en) * 1976-03-18 1977-09-21 Sony Corp Etching solution for plastics
US6512182B2 (en) * 2001-03-12 2003-01-28 Ngk Spark Plug Co., Ltd. Wiring circuit board and method for producing same
US20050199587A1 (en) 2004-03-12 2005-09-15 Jon Bengston Non-chrome plating on plastic
JP5552269B2 (en) * 2009-07-02 2014-07-16 トヨタ自動車株式会社 Electroless plating method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919768A (en) * 1989-09-22 1990-04-24 Shipley Company Inc. Electroplating process
US5160600A (en) * 1990-03-05 1992-11-03 Patel Gordhanbai N Chromic acid free etching of polymers for electroless plating
CN1508287A (en) * 2002-12-18 2004-06-30 Method for activating substrate for plating on plastic
LT2008082A (en) * 2008-10-28 2010-05-25 Chemijos Institutas Process for etching polyimide and other plastics
CN102409320A (en) * 2011-11-29 2012-04-11 沈阳工业大学 Electroplating pretreatment method for acrylonitrile butadiene styrene (ABS) plastic surface

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