RHODIUM-PLATED ARTICLE WITH BLACK OR BLUE COLOR, PROCESS FOR MAKING THE SAME AND BATH THEREFOR

Abstract: A rhodium-plated article with black or blue color is obtained through electroplating by using a plating bath comprising a conventional acid rhodium bath and an additive consisting of organocarboxylic acid, aromatic sulfonic acid or salts of these, amine, gelatine, butynediol, hypophosphite or a mixture thereof. The rhodium-plated article with the black color is subjected to anodic treatment for improving wear resistance.

Description: DESCRIPTION RHODUM-PLATED ARTICLE WITH BLACK OR BLUE COLOR, PROCESS FOR MAKING THE SAME AND BATH THEREFOR. BACKGROUND The present invention relates to a novel article which is plated with rhodium developing black or blue color, a process for making the same and a novel bath for rhodiumplating. All the colors of the platings which are obtainable through known rhodium-plating baths are white, the known rhodium baths comprising various rhodium salts, e.g., sulfate or phosphate. Rhodium-plating has been generally employed for use in electric contacts, iead frames and ornamental articles due to its good hardness, wear resistance, corrosion or erosion resistance and stability in the contact resistance. Furthermore, it has been desired to develop rhodium plating with different colors besides white, as it will enhance the practical value of the rhodium plating. On the other hand, known manners for black plating or black coloring such as black chrome plating, black nickel plating, blackening with copper carbonate all encounter difficulties in obtaining gioss, some of them yielding clouding, that is to say, these all being less valuable in the ornamental effect. There have been further problems in the manufacturing process, wherein they showed bad reproducibility in operation conditions, difficulties in mass production or the like. Thus there has been much to be desired in the prior art and it has long been desired to develop black color plating of noble metal in the ornamental article industries. SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a noble rhodium-plated article with black or blue color as well as mirror-like gloss. Another object of the present invention is to provide a process and a plating bath for making such rhodium-plated article with- black or blue color. A further object of the present invention is to provide a process for improving the wear resistance of the rhodium plating with the black color. Stiil further objects of the invention will become apparent from the disclosure hereinbelow. The inventors have become aware of the following fact after investigations for developing a bath composition for plating ("plating bath" or "bath" hereinafter) which provides a plating suitable for ornamental articles, particularly glasses, watches, accessories, cosmetics or dinner wares; rhodium-plating with black or blue color and m i rror- I i ke gloss is obtainable through a normal plating manner in an acid rhodium-plating bath comprising an additive consisting of at least one selected from the group consisting of organocarboxylic acid, aromatic sulfonic acid or salts of these, amine, gelatine, butynediol and hypophosphite, the resultant rhodium-plating providing good adhesion and good corrosion or erosion resistance. Based on such finding, the inventors have completed the present invention. It has been revealed that further improvement in the wear resistance of the black rhodium plating is obtainable through anodic electrolysis treatment (or "anodic treatment" hereinafter) of the rhodium-plated article with the black color. The rhodium-plated articles of the present invention are suitable for, e.g., frames or glasses, cases, faces and bands of watches, necktie pins, lighters, necklaces, rings, compacts, caps for lipsticks and the like. The articles of the present invention may be utilized not only in the ornamental purpose but in various fields which require such a good plated. coating. The present invention will be described hereinbelow with reference to preferred embodiments which will, however, serve to- better illustration of the invention and not to limitation thereof. Modifications may be done without aparting from the gist of the present invention. DETAILED DESCRIPTION OF THE INVENTION The plating bath of the present invention comprises a normal acid rhodium plating bath comprising rhodium salt and free acid (known per se), and an additive consisting of at least one selected from the group consisting of organocarboxylic acid, aromatic sulfonic acid or salts of these, amine, gelatine, butynediol and hypophosphite (referred to "additive" hereinafter). This plating bath is used for placing treatment of the articles resulting in rhodium-plated articles with desired properties. Normally, the plating bath comprising three ingredients of rhodium salt, free acid and the additive such as organocarboxylic acid hereinabove mentioned will be sufficient for accomplishing the purpose of the present invention. Rhodium salts which are normally used in the conventional rhodium plating, e.g., sulfate, phosphate, sulfamic acid and the like are employed as the rhodium salt for the plating bath. The rhodium salt concentration in the bath ranges within a conventional, normal concentration, i.e., from 0.1 g/l to 20 g/l. At a concentration below 0.1 g/I the speed of electrodesposition will be undesirably reduced. At a concentration exceeding 20 g/l the expensive rhodium would be used without effective utilization. The free acid encompasses acids which are normally used in the acid plating bath, such as sulfuric acid, phosphoric acid, sulfamic acid and the like. Among the. additives of the invention, organocarboxylic acid and aromatic sulfonic acid are used in either a free acid form or a salt form, only one of these being sufficient, however, two or more being applicable. The terms organocarboxylic acid or aromatic sulfonic acid denote also their salts hereinafter. Such salts encompass sodium or potassium salt. The concentration of organocarboxylic acid and/or aromatic sulfonic acid should be determined relating to the concentration of rhodium, and, however, be not less than 0.01 g/l, a lower concentration of which would deterioratingly affect upon color development. These additives may be added to the bath up to a solubility limit in the bath, however, used at a concentration which is practically sufficient. Organocarboxylic acid of the invention encompasses acetic acid and benzoic acid which have only one carboxylic group and no other functional group, phthalic acid and thiomalic acid which have two -carboxylic groups, and salts of each. The concentration of aromatic sulfonic acid in the bath approximates to that of organocarboxylic acid. Aromatic sulfonic acid encompasses benzenesulfonic acid, nitrobenzenesulfonic acid, phenosulfonic acid, metanilic acid or the like and salts of these acids. The additives to the bath in the present invention further encompasses amine, gelatine and butynediol. Amine encompasses ethy lenediami ne, triethanol amine, sulfuric hydroxylamine, diethylenetriamine or the like. One amine among those as the additive is sufficient, however two or more amines or amine(s) with other additives may be used. The concentration of amine2 gelatine and butynediol in the bath approximates to that of organocarboxylic acid. Hypophosphite as the additive encompasses alkali metal salts (sodium or potassium salt), alkaline earth metal salts (calcium or magnesium salt), other divalent metal salts (Co-, Ni-, Fe-, or Mn- salt) and the like. Among those salts alkali metal salts or alkaline earth metal salts are preferred. The concentration of hypophosphite as the additive in the bath approximately ranges from 0.5 to 10 g/l. A lower concentration less than 0.5 g/l does not develop sufficient effect, and that exceeding 10 g/l would cause to get cloudy, i.e., to loose the gloss. This additive of hypophosphite requires slightly different conditions of plating with respect to pH, bath temperature or the like from the other additives aforementioned. For hypophosphite the pH should be below 2.5 as a higher pH would cause cracks or precipitation in the bath. An optimum temperature for hypophosphite approximately ranges from 20 to 45 C. A higher temperature exceeding 450C is not preferred as it enhances the possibility of the partial clouding. However, the current density at a conventional, normal range (e.g°, approximately 0.5 - 5 A/dm2) may be adopted. The additives as hereinabove mentioned belong to essential ingredients of the bath according to the present invention, however, a further agent as a brightener may be added to the bath,. i.e. 0.1 - 10 mg/l or nonionic surfactant may be used. Such non ionic surfactant encompasses that of the ether -type, e.g. polyoxyethylene alkylèther, polyoxyethylenealkylphenylether or the like, which are generally used as the brightener in the prior art, however, further serve to inhibit the plating from forming microcracks, partial clouding and to produce a uniform color tone. Again turning to the additives of the invention other than hypophosphite, the pH value of the bath should not exceed 6. At a higher pH value than 6, rhodium in the bath will form hydroxide to form precipitation to disadvantage. The color of the rhodium-plated coating or film relates to the thickness thereof, wherein a thinner coating will produce blue color while a thicker coating black color. Provided that benzoic acid is used as organocarboxylic acid, the plating of the thickness less than 0.05 micron produces the blue color, whereas the thickness of 0.1 micron or more produces the black color, and the thickness between 0.05 and 0.1 micron will produce bluish black color. The thickness of 5 microns shows still the black color. Other organocarboxylic acid develops also the similar results in the color as well as the other additives aforementioned. In the practical operation, it is also affected by plating conditions, whether the plating becomes black or blue, the plating conditions encompassing concentrations in the bath of the rhodium salt and the additive(s), bath temperature current density, plating time, and the like. Such factors should be determined through a preparatory test plating under consideration such factors. In the practical plating procedure, the control: or choice of the color is preferably made mainly by changing the plating time under a predetermined bath condition. The bath temperature and current density for plating procedure are adopted within the values as adopted in the conventional manner. A bath temperature of 10 - 800C should be adopted. At a lower temperature less than 100C, the current density will not sufficiently rise resulting in the low electrodeposition efficiency. At a temperature higher than 80 C, the disadvantage of violent vaporization of the bath will overcome the advantage of enhancement in the electrodeposition efficiency. The current density having close relation with the color tone should be 0.1 10 A/dm2. A higher current density than 10 A/dm2 will cause violent evaporation of gas at a cathode in the bath accompanied by a deteriorated color tone. Materials for anode and cathode which are employed upon rhodium plating in the prior art may be used. The cathode may be selected from known material having a metallic surface such as brass, German silver (nickel silver), stainless steel or the like (however, iron, aluminium and zinc cannot be plated directly thereon). The cathode material further encompasses articles coated with strike (substrate coating), e.g., nickel strike or paradium-nickel strike. The cathode material encompasses also non-metallic articles coated with such substrate coating. One of insoluble electrodes is sufficient for the anode, e.g., platinum electrode, titanium electrode coated with platinum or platinum-rhodium plating. Other known manner generally applicable to the plating process may be optionally appiied in the plating procedure in the present invention. The article thus obtainable according to the present invention, however, has the mirror-like gloss with its surface, the black or blue color, good adhesion, good corrosion or erosion resistance, and the hardness compatible with the conventional rhodium plated articles without applying other conventional agents for various purposes. In other words, the rhodium-plated article with the black or blue color is obtainable through applying a bath essentially consisting of three ingredients, i.e., rhodium salt, free acid and the additive of the invention, the additive being organocarboxylic acid, aromatic sulfonic acid or one of other members aforementioned. Thus the present invention is applicable in the industries with advantage. Further development of the present invention is accomplished through applying anodic electrolysis treatment (or so-called anodic treatment) to the rhodium-plated article with the black color resulting in the improvement in the wear resistance and adhesion as we as the blackness. Plated articles with the black color to be treated through the anodic treatment are those which were rhodiumplated on the surface and have the black color as aforementioned. General manners for the anodic treatment, known per se, may be employed in the anodic treatment of the invention. A bath for this treatment is such that accompanies a reaction generating oxygen, provided that the plated coating or substrate of plating should not be corroded or eroded upon dipping the articles for treatment or during the treatment. Thus, strong acid such as sulfuric acid, hydrochloric acid, nitric acid or the like, and strong alkali such as sodium hydroxide and potassium hydroxide are not preferred. Electrolyte applicable to the anodic treatment encompasses organic and inorganic substances either alone or in combination. The pH value and the temperature of the bath for anodic treatment may be adopted according to such conditions that are applicable in the conventional plating or electrolytic treatment. Counted as the electrolyte for such purpose are as follows: organic acid such as citric acid, glutamic acid, tartaric acid, acetic acid, stearic acid, lactic acid, succinic acid, sulfamic acid,. or salts thereof with sodium, potassium or ammonium; inorganic acid such as pyrophosphoric acid, phosphoric acid, carbonic acid, cyanic acid, boric acid, silicic acid, or salts of - these inorganic acids; methyl alcohol, ehtyl alcohol, ethyleneglycohol, benzilamine, cycrohexane, EDTA, sodium saccharinate, pol yacrylamide, or polyethylene imine. Upon the anodic treatment, an insoluble cathode of known nature, e.g., platinum, titanium-rhodium allby, titanium-platinum alloy, stainless steel, carbon or the like may be employed. The anodic treatment of the present invention is successfully effected, e.g., under the following conditions: a bath temperature at 30 - 60 C, a concentration of the electrolyte at 1Q - 100 g/l, a current density of 0.1 - 20 A/dm2 and a treating period of 3- 60 minutes. However, deviation from these conditions may be done optionally. The composition of the bath generally affects upon the bath potential, anode current density and treating time, which makes it necessary to choose each optimal condition for each treating bath, thus such treatment conditions cannot be unconditionally or generally determined without specifying the bath composition. This reason is understood by that the oxygen overvoltage for each electrolyte is different. For instance, provided that a bath comprising 50 g/l sodium citrate is used, the anode current density of not less than 0.1 A/dm2 is sufficient at a treatment time of three minutes, whereas a shorter treatment time suffices at a higher. current density, or a longer treatment time is applied if the current density is small. The concentration of the electrolyte in the bath is so adopted that oxygen can be released at the anode, which concentration widely ranges, e.g., from a few g/l to that of the upper solubility limit. Accordingly, the present invention also provides the rhodium-plated articles having the practically sufficient wear resistance and the enhanced blackness through the anodic treatment of the rhodium-plated articles as aforementioned. Now, in the followings, the present invention will be described in more detail by way of preferred embodiments thereof, which will not serve to limitation of the invention. EXAMPLE 1. In a bath of pH 4.0 obtained by mixing rhodium sulfate (rhodium: 4 g/l), phthalic acid (2 g/l) and sulfuric acid were set a titanium anode plated with platinum and a cathode of a brass watch case plated with a nickel strike. The watch case was electroplated for ten minutes under conditions of a bath temperature of 30 C and a current density of 0.5 A/dm2. The resultant plating film presented black color and mirror-like gloss provided with 0.3 micron thickness and good adhesion. The same article was electroplated for one minute under the same conditions. The resultant plating film was 0.03 micron thick provided with mirror-like gloss and blue color. The resultant watch case was tested with respect to the corrosion resistance through a CAS-testing manner and exposure testing in an ammonia atmosphere. No corrosion was observed thus exhibiting the good corrosion resistance. The articles showed a hardness compatible with the level of the rhodium-plated white coating according to the conventional manner. v N . B . exposure in the ammonia atmosphere: Example pieces were put in a desiccator, charged with ammonia water of the density 0.96 on the bottom, the sample pieces were kept therein at 200C for 24 hours exposed to an ammonia atmosphere. After the exposure, color change and bulging on the surface were observed. EXAMPLES 2 - 8. Rhodium-plating was carried out under the conditions as shown in Table I otherwise in the same condition as disclosed in Example 1, the results being also disclosed in Table 1. All the sample pieces showed properties equivalent to those of Example 1 with respect to the mirror-like gloss, corrosion resistance, hardness and adhesion. Table 1 EMI18.1 bath <SEP> current <SEP> plating <SEP> plating <tb> Example <SEP> bath <SEP> concentration <tb> temperature <SEP> density <SEP> cathode <SEP> time <SEP> thickness <SEP> color <tb> No. <SEP> composition <SEP> g/l <tb> C <SEP> A/dm2 <SEP> min. <SEP> <tb> Rh-sulfate <SEP> (Rh) <SEP> 4 <SEP> 30 <SEP> 0.5 <SEP> stainless <SEP> steel <SEP> 20 <SEP> 0.4 <SEP> black <tb> 2 <SEP> benzoic <SEP> acid <SEP> 2 <SEP> frame <SEP> of <SEP> glasses <tb> sulfuric <SEP> acid <SEP> total <SEP> 12 <SEP> " <SEP> " <SEP> with <SEP> Pd-Ni <SEP> strike <SEP> 2 <SEP> 0.04 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 50 <SEP> 2 <SEP> stainless <SEP> steel <SEP> 10 <SEP> 0.2 <SEP> black <tb> 3 <SEP> thiomalic <SEP> acid <SEP> 1 <SEP> necktie <SEP> pin <SEP> with <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> " <SEP> " <SEP> Ni <SEP> strike <SEP> 1.5 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 50 <SEP> 0.5 <SEP> 5 <SEP> 0.2 <SEP> black <tb> brass <SEP> plate <SEP> with <tb> 4 <SEP> acetic <SEP> acid <SEP> 20m@/@ <SEP> Ni <SEP> strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> " <SEP> 1 <SEP> 1 <SEP> 0.04 <SEP> blue <tb> Rh-phosphate <SEP> (Rh) <SEP> 4 <SEP> 50 <SEP> 1 <SEP> 20 <SEP> 0.5 <SEP> black <tb> brass <SEP> plate <tb> 5 <SEP> K-benzoate <SEP> 3 <SEP> (10 <SEP> cm2) <tb> phosphoric <SEP> acid <SEP> total <SEP> 12 <SEP> " <SEP> " <SEP> 2 <SEP> 0.05 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <tb> k-phthalate <SEP> 1 <SEP> 30 <SEP> 0.5 <SEP> brass <SEP> plate <SEP> with <SEP> 20 <SEP> 0.3 <SEP> black <tb> 6 <tb> k-benzoate <SEP> 2 <SEP> Pd-Ni <SEP> strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <tb> Rh-sulphate <SEP> (Rh) <SEP> 2 <SEP> 50 <SEP> 1 <SEP> flash <SEP> gold <SEP> plated <SEP> 10 <SEP> 0.1 <SEP> black <tb> 7 <SEP> Na-acetate <SEP> 30 <SEP> German <SEP> silver <tb> sulfuric <SEP> acid <SEP> total <SEP> 12 <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 50 <SEP> 0.5 <SEP> 1 <SEP> 0.02 <SEP> blue <tb> 8 <SEP> k-thiomalate <SEP> 25 <SEP> brass <SEP> plate <tb> sulfuric <SEP> acid <SEP> total <SEP> 50 <tb> EXAMPLE 9. In a bath obtained by mixing rhodium sulfate (rhodium: 2 g/I), o-nitrobenzenesulfonic acid (10 g/l) and sulfuric acid (total: 6 g/l) were set the same anode as used in Example 1 and a cathode of a stainless steel watch case with a nickel strike. The watch case was electroplated for 10 minutes under conditions of a bath temperature of 500C and the current density at 1 A/dm2. The resultant plating film presented black color with mirror-like gloss. The film was 0.5 micron thick having good adhesion. After one minute electroplating otherwise under the same conditions, a 0.05 micron thick plating with mirror-like gloss was obtained. Testing in the manner as disclosed in Example 1 revealed the good corrosion resistance and a hardness compatible with conventional white rhodium plating. EXAMPLES 10 - 17. Rhodium plating was carried out under conditions as shown in Table 2 otherwise under the same conditions as disclosed in Example 9, the results being also disclosed in Table 2. The resultant platings showed mirror-like gloss, the good corrosion resistance and hardness. Table 2 EMI21.1 bath <SEP> current <SEP> plating <SEP> plating <tb> Example <SEP> bath <SEP> concentration <tb> temperature <SEP> density <SEP> cathode <tb> time <SEP> thickness <SEP> color <tb> No. <SEP> composition <SEP> g/l <tb> C <SEP> A/dm2 <SEP> min. <SEP> <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> stainless <SEP> steel <SEP> 20 <SEP> 0.15 <SEP> black <tb> benzenesulfonic <SEP> frame <SEP> of <SEP> glasses <tb> 10 <SEP> 50 <SEP> 1 <tb> acid <SEP> 10 <SEP> with <SEP> Pd-Ni <SEP> strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> 5 <SEP> 0.04 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 4 <SEP> brass <SEP> plate <SEP> 10 <SEP> 0.14 <SEP> black <tb> 11 <SEP> metanilic <SEP> acid <SEP> 1 <SEP> 50 <SEP> 2 <SEP> with <SEP> Ni <SEP> strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 30 <SEP> 2 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 10 <SEP> 0.35 <SEP> black <tb> o-phenolsulfonic <tb> 12 <SEP> 50 <SEP> 0.5 <SEP> brass <SEP> plate <tb> acid <SEP> 1 <tb> sulfuric <SEP> acid <SEP> total <SEP> 45 <SEP> 1 <SEP> - <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 4 <SEP> 5 <SEP> 0.6 <SEP> black <tb> gold <SEP> flash Na-o-nitro13 <SEP> 30 <SEP> 2 <SEP> plated <SEP> brass <SEP> plate <tb> benzenesulfonate <SEP> 15 <tb> sulfuric <SEP> acid <SEP> total <SEP> 40 <SEP> 1/4 <SEP> - <SEP> blue <tb> Rh-phosphate <SEP> (Rh) <SEP> 2 <SEP> 5 <SEP> 0.3 <SEP> black <tb> stainless <SEP> watch <tb> 14 <SEP> Na-benzenesulfonate <SEP> 15 <SEP> 50 <SEP> 1 <tb> case <SEP> with <SEP> Ni <SEP> strike <tb> phosphoric <SEP> acid <SEP> total <SEP> 50 <SEP> 1/2 <SEP> - <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 10 <SEP> 0.3 <SEP> black <tb> frame <SEP> of <SEP> glasses <tb> 15 <SEP> K <SEP> -metanilate <SEP> 1 <SEP> 50 <SEP> 1 <tb> with <SEP> Pd-Ni <SEP> strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 12 <SEP> 1 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 3 <SEP> 5 <SEP> 0.6 <SEP> black <tb> Na-o-phenol16 <SEP> 60 <SEP> 1 <SEP> brass <SEP> plate <tb> sulfonste <SEP> 1 <tb> sulfuric <SEP> acid <SEP> total <SEP> 50 <SEP> 1/2 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 5 <SEP> 0.35 <SEP> black <tb> Na-benzenesulfonate <SEP> 10 <tb> brass <SEP> plate <SEP> with <tb> 17 <SEP> Na-o-phenol- <SEP> 50 <SEP> 0.5 <tb> Ni <SEP> strike <tb> sulfonate <SEP> 0.5 <SEP> 1/2 <SEP> 0.04 <SEP> blue <tb> sulfuric <SEP> acid <SEP> total <SEP> 50 <tb> EXAMPLE 18. Electroplating with rhodium was carried out under the conditions as shown in Table 3, otherwise under the same condition as in Example 1. The resultant plating film was 0.1 micron thick having good adhesion. The good corrosion resistance was exhibited through the same testing as in Example 1, and the hardness compatible with the conventional white rhodium plating was exhibited. By electroplating for 4 minutes otherwise under the same conditions as above,. the resultant plating developed blue color provided with the thickness of 0.02. micron and other good properties as in the black rhodium plating. EXAMPLES 19 - 23. Rhodium plating was carried out under conditions as shown in Table 3 otherwise under the same conditions as in Example 1, the results being also disclosed in Table 3. The resultant platings showed the mirror-like gloss, the good corrosion-resistance and hardness as in Example 18. Table 3 EMI23.1 bath <SEP> current <SEP> plating <SEP> plating <tb> Example <SEP> bath <SEP> concentration <tb> temperature <SEP> density <SEP> cathode <SEP> time <SEP> thickness <SEP> color <tb> No. <SEP> composition <SEP> g/l <tb> C <SEP> A/dm2 <SEP> min. <SEP> <tb> Rh-sulfonate <SEP> (Rh) <SEP> 2 <SEP> stainless <SEP> watch <SEP> 20 <SEP> 0.1 <SEP> black <tb> 18 <SEP> triethanolamine <SEP> 1 <SEP> ml/l <SEP> 50 <SEP> 0.5 <SEP> case <SEP> with <SEP> Ni <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> strike <SEP> 4 <SEP> 0.02 <SEP> blue <tb> Rh-phosphate <SEP> (Rh) <SEP> 2 <SEP> stainless <SEP> watch <SEP> 5 <SEP> 0.3 <SEP> black <tb> 19 <SEP> ethylenediamine <SEP> 50 <SEP> ml/l <SEP> 50 <SEP> 2 <SEP> case <SEP> with <SEP> Niphosphoric <SEP> acid <SEP> total <SEP> 50 <SEP> Pd <SEP> strike <SEP> 1/2 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 10 <SEP> 0.38 <SEP> black <tb> brass <SEP> plate <SEP> with <tb> 20 <SEP> gelatine <SEP> 0.4 <SEP> 30 <SEP> 2 <tb> Ni-strike <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> 1 <SEP> 0.04 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 2 <SEP> 5 <SEP> 0.3 <SEP> black <tb> 21 <SEP> butynediol <SEP> 2 <SEP> 50 <SEP> 2 <SEP> brass <SEP> plate <tb> sulfuric <SEP> acid <SEP> total <SEP> 6 <SEP> 1/2 <SEP> 0.03 <SEP> blue <tb> Rh-sulfate <SEP> (Rh) <SEP> 3 <tb> 22 <SEP> Na-hypophosphite <SEP> 1 <SEP> 25 <SEP> 3 <SEP> brass <SEP> plate <SEP> 10 <SEP> 0.5 <SEP> black <tb> sulfuric <SEP> acid <SEP> free <SEP> 10 <tb> Rh-sulfate <SEP> (Rh) <SEP> 3 <tb> 23 <SEP> Co-hypophosphite <SEP> 1 <SEP> 25 <SEP> 3 <SEP> brass <SEP> plate <SEP> 10 <SEP> 0.5 <SEP> black <tb> sulfuric <SEP> acid <SEP> free <SEP> 10 <tb> Rh-sulfuric <SEP> acid <SEP> (Rh) <SEP> 3 <tb> 24 <SEP> Ni-hypophosphite <SEP> 1 <SEP> 25 <SEP> 3 <SEP> brass <SEP> plate <SEP> 10 <SEP> 0.5 <SEP> black <tb> sulfuric <SEP> acid <SEP> free <SEP> 10 <tb> EXAMPLES 31 - 37. The rhodium-plated brass plate with the black color and the thickness of 0.3 micron which was obtained in Example 1 was subjected to anodic treatment under conditions disclosed in Table 4. The resultant sample pieces were tested with respect to the surface conditions such as the wear resistance, color difference, gloss and the like. The results are shown in Table 5. The wear resistance was measured by rubbing the 2--- sample plate surface of 10 cm on a backside of the cow leather under the application of 600 g load at a reciprocal movement speed of 1 cycle/second. The color difference and gloss were measured according to the measuring method of mirror surface gloss, JIS Z 8741-1978 "gloss measurement method" by using a color difference meter of Nippon Denshoku Kogyo K.K. (type ND-5). The smaller is the value, the deeper or stronger blackness is represented. As is shown in these results, the rhodium-plated article with the good wear-resistance and the much stronger blackness is obtainable according to these embodiments. EXAMPLE 38. The resultant article as obtained in Example 2 having the 0.4 micron thick plating provided with the black mirror-like gloss was subjected to the anodic treatment under the same condition as in Example 31, resulting in the same good properties as in Example 31. Table 4 EMI26.1 bath <SEP> bath <SEP> current <SEP> treating <tb> Example <SEP> concentration <tb> temperature <SEP> potential <SEP> density <SEP> DA <SEP> time <tb> electrolyte <tb> No. <SEP> g/l <SEP> C <SEP> V <SEP> A/dm2 <SEP> min. <tb> 31 <SEP> Na-citrate <SEP> 50 <SEP> 50 <SEP> 6 <SEP> 6 <SEP> 3 <tb> 32 <SEP> phosphoric <SEP> acid <SEP> 10 <SEP> 40 <SEP> 3 <SEP> 4.5 <SEP> 5 <tb> 33 <SEP> acetic <SEP> acid <SEP> 50 <SEP> 30 <SEP> 10 <SEP> 0.5 <SEP> 45 <tb> ammonia <SEP> water <tb> 34 <SEP> 30 <SEP> ml/l <SEP> 20 <SEP> 10 <SEP> 0.3 <SEP> 30 <tb> (28 <SEP> %) <tb> 35 <SEP> tartaric <SEP> acid <SEP> 10 <tb> ammonium <SEP> 50 <SEP> 3 <SEP> 0.2 <SEP> 3 <tb> tartarate <SEP> 10 <tb> Na-glutamate <SEP> 10 <tb> 36 <SEP> 30 <SEP> 6 <SEP> 1.5 <SEP> 5 <tb> K-phthalate <SEP> 10 <tb> triethanolamine <SEP> 25 <SEP> ml/l <tb> 37 <SEP> 30 <SEP> 6 <SEP> 2.5 <SEP> 5 <tb> Na-acetate <SEP> 50 <tb> Table 5 EMI27.1 wear <SEP> resistance <SEP> surface <SEP> conditions <tb> Example <tb> wear <SEP> color <SEP> difference <SEP> gloss <SEP> Remarks <tb> No. <SEP> evaluation <tb> mg/1000 <SEP> times <SEP> (L) <SEP> ( <SEP> % <SEP> ) <tb> 31 <SEP> 0 <SEP> good <SEP> 18.9 <SEP> 409 <tb> 32 <SEP> 0.1 <SEP> " <SEP> 18.4 <SEP> 403 <tb> 33 <SEP> 0 <SEP> " <SEP> 18.0 <SEP> 397 <tb> 34 <SEP> 0 <SEP> " <SEP> 18.5 <SEP> 405 <tb> 35 <SEP> 0.2 <SEP> " <SEP> 19.1 <SEP> 410 <tb> 36 <SEP> 0 <SEP> " <SEP> 18.9 <SEP> 408 <tb> 37 <SEP> 0 <SEP> " <SEP> 18.3 <SEP> 402 <tb> Example <SEP> 1 <SEP> before <tb> R38 <SEP> 5.6* <SEP> bad <SEP> 25.9 <SEP> 508 <SEP> anodic <SEP> treatment <tb> * <SEP> mg/200 <SEP> times <tb> R39 <SEP> 0 <SEP> good <SEP> 34.4 <SEP> 976 <SEP> white <SEP> rhodium <SEP> plating <tb> EXAMPLE 39 - 45. Phthalic acid (2 g/l) in Example 1 was replaced with metanilic acid (I g/l), under which condition rhodium plating was effected otherwise under the same condition as in Example 1. The resultant sample pieces were treated as in Examples 31 - 37, resulting in the same good properties as in Example 31 - 37. EXAMPLE 46. Benzoic acid (2 g/l) in Example 2 was replaced with ethylenediamine (50 ml/1), under which condition otherwise the same conditions as in Example 2 rhodium plating was effected. The resultant sample pieces were treated as in Example 38, resulting in the same good properties as in Example 38. EXAMPLE 47. The same rhodium-plated brass plate as used in Example 31 (thus Example 1) was subjected to anodic treatment under conditions of electrolyte composition, concentration and electrolysis conditions as shown in Table 6 otherwise in the same manner as in Example 31. The resultant pieces showed rhodium-plating films with the enhanced blackness and wear resistance. Table 6 EMI29.1 bath <SEP> current <SEP> bath <SEP> treating <tb> concentration <tb> electrolyte <SEP> temperature <SEP> density <SEP> potential <SEP> time <tb> g/l <SEP> C <SEP> A/dm2 <SEP> V <SEP> min <tb> K-cyanate <SEP> 50 <SEP> 50 <SEP> 9.0 <SEP> 6 <SEP> 3 <tb> boric <SEP> acid <tb> 50 <SEP> + <SEP> 50 <SEP> 50 <SEP> 2.5 <SEP> 6 <SEP> 3 <tb> + <SEP> Na-borate <tb> ammonium <SEP> citrate <SEP> 50 <SEP> 50 <SEP> 5.5 <SEP> 6 <SEP> 3 <tb> citric <SEP> acid <SEP> 50 <SEP> 50 <SEP> 1.0 <SEP> 6 <SEP> 3 <tb> Phosphoric <SEP> acid <SEP> 50 <SEP> 50 <SEP> 4.5 <SEP> 6 <SEP> 3 <tb> acetic <SEP> acid <SEP> 50 <SEP> 50 <SEP> 0.5 <SEP> 6 <SEP> 5 <tb> 0.02 <tb> Na-citrate <SEP> 100 <SEP> 25 <SEP> 1 <SEP> # <SEP> 5 <SEP> 1 <SEP> # <SEP> 10 <tb> #0.5 <tb> 0.004 <tb> polyetheleneimine <SEP> 20 <SEP> 25 <SEP> 2 <SEP> # <SEP> 7.8 <SEP> 10 <SEP> # <SEP> 20 <tb> #0.02 <tb>

Claims: CLAIMS 1. A rhodium-plated article with black or blue color. 2. A process for producing a rhodium-plated article with black or blue color which comprises: a step for preparing a rhodium plating bath comprising normal acid bath of rhodium and an additive consisting of at least one selected from the group consisting of organocarboxylic acid, aromatic sulfonic acid or salts of these, amine, gelatine, butynediol and hypophosphite, and a step of electroplating an article in said rhodium plating bath under such conditions that the rhodium plating film develops black or blue color. 3. An acid rhodium plating bath for producing a rhodium-plated article with black or blue color which comprises: a normal acid bath or rhodium and an additive consisting of at least one selected from the group consisting of organocarboxylic acid, aromatic sulfonic acid or salts of these, amine, gelatine, butynediol and hypophosphite. 4. A process for producing a rhodium-plated article with black color and good wear resistance which comprises a step of subjecting a rhodium-plated article with black color to anodic treatment. 5. The rhodium-plated article as defined in Claim 1, wherein the thickness of the rhodium plating film is from 0.02 to 5 microns. 6. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein organocarboxylic acid is organomonocarboxyl ic acid having one carboxyl group. 7. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein organocarboxylic acid is that having at least two carboxyl groups. 8. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein organocarboxylic acid is that having an amino group. 9. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3,- wherein organocarboxylic acid is that having no sulfonic acid group. 10. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein organocarboxylic acid is aromatic carboxylic acid. 11. The process as defined in Claim 2 or the.rhodium plating bath as defined in Claim 37 wherein organocarboxylic acid is one selected from the group consisting of benzoic acid, acetic acid, thiomalic acid, phthalic acid and salts thereof. 12. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein aromatic sulfonic acid is that having one sulfonic acid group. 13. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein aromatic sulfonic acid is a benzene derivative. 14. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein aromatic sulfonic acid is one selected from the group consisting of benzenesulfonic acid, nitro benzenesulfonic acid, phenolsulfonic acid, metanilic acid, and salts thereof. 15. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein amine is ethylenediamine; triethanolamine, sulfuric hydroxylamine, diethylenetriamine or a mixture thereof. 16. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein hypophosphite is alkali metal salt, alkaline earth metal salt, divalent metal salt other than alkaline earth metal salt, or a mixture thereof. 17. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein said rhodium plating bath has a pH value not exceed ing 6. 18. The process as defined in Claim 2 or the rhodium plating bath as defined in Claim 3, wherein said additive is hypophosphite and the pH value of the bath is not exceeding 2.5. 19. The process as defined in Claim 2 or the rhodium plating bath as defined in. Claim 3, wherein said rhodium plating bath substantially consisting of rhodium salt, free acid and said additive. 20. The process as defined in Claim 4, wherein the anodic treatment is carried out under such conditions that the rhodium plating film andjor substrate are/is not corroded. 21. The process as defined in Claim 4, wherein the anodic treatment is carried out in a bath comprising one or more electrolyte(s)- selected from the group consisting of organic and inorganic acid or salts thereof except for strong acid, methylalcohol, ethylalcohol, ethylene glycohol, benzilamine, cyclohexane, ETDA, sodium saccarinate, polyacrylamide and polyethylene imine. 22. The process as defined in Claim 21, wherein the organic acid is one or more selected from the group consisting of citric acid, glutamic acid, tartaric acid, acetic acid, stearic acid, lactic acid, succinic acid, sulfamic acid and salts thereof. 23. The process as defined in Claim 21, wherein the inorganic acid is one or more selected from the group consisting of pyrophosphoric acid, phosphoric acid, carbonic acid, cyanic acid, boric acid, silicic acid any salts thereof. 24. The process as defined in Claim 4, wherein the rhodium-plated article with black color is one produced through the process as defined in Claim 2. 25. A product obtained through the process as defined in Claim 4 or Claim 21.

Inventors: ICHIMURA, SEIJI, KINASE, TAKASHI, KINJO, YOSHIO, MASHIKO, MASAYOSHI, MATSUMOTO, YOSUKE, SUZUKI, KEJIRO
Applicants: NIPPON METAL PLATING CO., LTD, NIPPON MINING COMPANY LIMITED
Application year: 1981
Main classification: C25D3
IPC codes: C25D11, C25D3