US2938805A - Process of stabilizing autocatalytic copper plating solutions - Google Patents

Process of stabilizing autocatalytic copper plating solutions Download PDF

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US2938805A
US2938805A US725451A US72545158A US2938805A US 2938805 A US2938805 A US 2938805A US 725451 A US725451 A US 725451A US 72545158 A US72545158 A US 72545158A US 2938805 A US2938805 A US 2938805A
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solution
copper
solutions
plating
gas
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Maynard C Agens
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General Electric Co
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General Electric Co
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • 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
    • C23C18/38Coating with copper
    • C23C18/40Coating with copper using reducing agents
    • C23C18/405Formaldehyde

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  • the present invention relates to a process for stabilizing copper plating solutions used to autacatalytiaclly plate copper onto metals or onto non-metallic surfaces. More particularly, this invention relates to a stabilization process which comprises producing oxidizing conditions within said plating solutions whereby the formation of cuprous oxide, which causes these solutions to become unstable, is greatly minimized or substantially prevented without the prevention of the reducing reaction which causes the copper to plate.
  • Cahill discloses complexing agents which are tartrates and salicylates used in the presence of carbonates all of which are water soluble.
  • Lukes discloses in his application S.N. 725,450 complexing agents which are ethyleneaminoacetic acids which are selected from the class consisting of ethylenediaminetetraacetic acid, diethylenetriaminepentaacetic acid and 1,2-cyclohexylenediaminetetraacetic acid.
  • S.N. 725,452 discloses complexing agents which are tartrates and salicylates used in the presence of carbonates all of which are water soluble.
  • Lukes discloses in his application S.N. 725,450 complexing agents which are ethyleneaminoacetic acids which are selected from the class consisting of ethylenediaminetetraacetic acid, diethylenetriaminepentaacetic acid and 1,2-cyclohexylenediaminetetraacetic acid.
  • S.N. 725,452 discloses complexing agents which are tartrates
  • R is a substituent selected from the group consisting of hydrogen and methyl, m is an integer and is at least 1 and no more than 4, n is an integer and is at least 0 and no more than 3, p is an integer and is at least 0 and not more than 1.
  • Equation II Since the reaction expressed by Equation II does not require activation by an extraneous material, it will occur merely upon the solution standing at room temperature and is hastened by heating.
  • the cuprous oxide product is reduced by the alkaline formaldehyde solution to copper metal which is one of the metals that is catalytically active in initiating the plating reaction expressed by Equation 1. Therefore, the reaction of Equation Ilcauses these solutions to spontaneously decompose and'to become useless upon standing for long periods.
  • the complexing agents used in any of the above copending applications greatly suppress the reaction expressed by Equation 11, nevertheless, high concentrations of cupric ion andthe high alkalinity of the solutions over-ride some of the efiect of these complexing agents. Furthermore, it is not possible to completely suppress Equation H with any complexing agent.
  • My invention comprises aerating these solutions with an oxygen'containing gas during storage or other periods of nonuse, and also while it is being used to plate copper. Aeration can be accomplish with pure oxygen or oxygen diluted with any inert gas such as argon, neon, krypton, nitrogen, and the like,'the simplest gaseous mixture to use being air itself even though it does contain a minor amount of carbon dioxide which reacts with the alkali in the solution.
  • the copper must be removed from contact with the solution, for example by filtration, centrifugation, decantation, etc. Furthermore, I have found that best results are obtained Ijhave the gas dispersed a s'very fine bubbles which areuuniformly distributed throughout the entire solution. Should, I fail to do this, I have noticed'that precipitation will occur in those-portions of the'solution not contacted by the gas, stream. Immediate correction of this condition can be effected by vigorous agitation. I have found that the best method of carrying my invention into effect is 'tointroduce the oxygen containing gas stream through a disperser such as a fritted glass disk or a po-' rous. ceramic disk so that the gas is.
  • a disperser such as a fritted glass disk or a po-' rous. ceramic disk so that the gas is.
  • the gas inlet and disperser must'be non-metals.
  • more than one stream of gas can be introduced into the solution; Providing the gas inlets are properly placed, and the volume oftheincoming gas is sufiicient, no further agitation is required since the gas streams themselves will provide suflicient agitation of the solution.
  • the entire liquid phase should be saturated with theoxygencontaining gas at all times. Filters can be used in conjunction with the aeration to' remove any solid material. Superatmospher-ic gas pressure can be'used but is undequired. Sub-atmospheric pressure is not desirable since it does not permit as elfective saturation of the solution with the oxygen-containinggas as do higher pressures. 1
  • aeration can be accomplished by flowing thin films of the plating solutions over the surfaces to be plated. By this means, a small volume of l-iquidis exposed to a large volume of oxygen-containing gas. .By inclining the surfaces so that the liquid flows rapidly, agitation is also provided.
  • the surfaces to be plated can be arranged in a stepwise fashion so that the liquid cascades from one surface to the nextinseries. If non-metallic'spray equipment is used, the plating solu tion can be sprayed as'anatomized 'm'istv to provide aera tion. In anyof these applications, if a reservoir ofliquid is present, additional. aeration of the liquid in the rese'r can; also be installed 1 1112118 line to remove any solid material; 1
  • the container for the plating solutions should s r am 4 be 9 arreassd a he e t gases o n t a -T a ma t than the amount of reagents.
  • some loss of formaldehyde will always occur, due to its volatilization in the gas stream. This loss can be compensated for by additions of aqueous formaldehyde continuously or at prescribed intervals so as to maintain the concentration required to produce the plating reaction.
  • Example 1 One liter of a plating solution was made by dissolving the following ingredients in enough water to make one liter of solution:
  • Theabove solution was divided into. two portions; one portion was used asa control and was allowed to standat room'temperature without any further treatment. The other portion was aerated by introduction of 'air into: the solution through a fritted glass disk. It was not mechanically stirred. At the end of approximately two hours, the control hadst'arfed'to decompose, as evidenced by the precipitationofi'copper. The aerated sample remained clear and unchanged. After leaving the solutions overnight; the control .sample had completely decomposed, as evidenced by the solution being colorless and all of the copper being a precipitate in the bottom of the'contain'er.
  • the aerated sample still blue in color and had apH of 11.5,; There was a smali' amou'nt of copper metal pres.- entin the'solution indicatingrthat the solution 'had not been well stirred.
  • a pieceof'sand-bl-asted paper-base, phenolic-resin laminate was sensitized by immersing it for one minute in a stannous chloride solution 'made by dissolving l0 gra'rns of stannouschlon'de and 10 milliliters of 12 molar hydrochloricacid in one liter of water, rinsed with water, dipped for oneminute into.
  • a' palladium chloride solution made by 'dissolvingdigram of palladium chloride and IOmillilite'rs of'l2- molar'hydrochloric' acid in one liter of water, andgagain rinsed in water.
  • Example 2 The solution as described in. Example 1 was duplicared d vid d im worortio n n p io a of nitrogen was adniitted atthe rate of 0.4 cubic foot per home; In the-second port-ion, a flow of pure en Wfl5 4mi s1 et-t a o 0-4 c t p hour.
  • Example 3 Two liters of solution were prepared containing the following ingredients in the stated concentrations:
  • a piece of paper-base, phenolic-resin laminate having an area of 50 sq. inches which had been sensitized with palladium as in Example '1 was placed in this solution. Air was bubbled in through a fritted glass filter diifuser at the rate of 0.2 liter per minute, while the solution was stirred vigorously with a mechanical stirrer. At the end of 5 hours an additional 25'milliliters of formaldehyde was added and 2 milliliters of a wetting agent comprising an ethylene oxide and propylene oxide polymer was added. The thickness of the copper coating was 0.6 to 0.7 mil thick and no decomposition of the plating solution had occurred.
  • the solution was plating satisfactorily and was left overnight, for 15 hours. No decomposition of the solution occurred during this time and the solution was still plating, however, at a very slow rate.
  • An additional 50 milliliters of formaldehyde was added and enough potassium hydroxide was added to increase the initial molarity of the base by an additional 0.80. This caused the solution to start plating rapidly again.
  • the solution was still plating at a rate of about 0.1 mil per hour and the total thickness of the copper plate was about 2 /2 mils.
  • the plating reaction was stopped at this point by acidifying the solution to a pH of 2, whereby 56 of the original 60 grams of the ethylenediaminetetraacetic acid was recovered by filtration of the solution, since this reagent is insoluble in the reaction mixture at this pH.
  • Example 4 One liter of solution was made containing the following ingredients:
  • both the first and third solutions which had not been aerated were starting to decompose as was evidenced by the formation of precipitate of cup'rous oxide.
  • Both the second and fourth solutions were still clear, with no evidence of decomposition at the end of 7 hours.
  • Example 5 A plating composition comprising three solutions useful in making copper mirrors was made up as follows.
  • Aqueous formaldehyde (37%) ml 80 Water ml 1250 The three solutions combined in the proportion Solution A ml Solution B ml 850 Solution C ml 1330
  • the resulting plating solution was divided into two portions. One portion was aerated with air at the rate of 0.5 cubic foot per hour while the other portion was permitted to stand at ambient temperature as a control.
  • a piece of paper base-phenolic-resin laminate that had been sensitized with palladium as in Example 1 was placed in each of the two portions copper plated onto the sensitized area. The pieces of laminate were removed and the solutions allowed to stand overnight.
  • the non-aerated sample had formed a smooth mirror over the entire area of the glass beaker contacted by the solution which was now depleted of copper. No sensitization of the non-metallic (glass) surface is necessary with this solution to obtain the mirror.
  • the aerated sample had not decomposed either by forming a copper mirror or by precipitating cuprous oxide. At the end of three days it was still stable and plated copper on the sensitized laminate. By stopping the aeration of a sample of this solution, a copper mirror will form on the walls of the container on standing overnight.
  • Example 6 One liter of solution was made containing the following concentration of ingredients:
  • Formaldehyde (37% aqueous sol.), 80 ml.
  • Example 7 One liter of solution was made containing the follow ing ingredients in the stated concentration:
  • Example 6 The procedure of Example 6 was repeated with almost identical results. The test for the aerated sample was discontinued at the end of eight hours with no sign of decomposition.
  • Example 8 In order to obtain some explanation as to the function of oxygen in preventing the decomposition of these platr 7 ing solutions, a solution was made up containing the following ingredients in the stated concentrations:
  • my method of stabilization is applicable to all plating solutions which are based on the reactionof formaldehyde. with a cupric salt complex in an alkaline solution :to. produce a film of' copper metal.
  • Thisrstabilizationv is apparently caused by the abilitylof the oxygen-containing gas to prevent the precipitation or, formation ofic'uprous oxide by thefsec ondary reaction outlined above.
  • the process for stabilizing aqueous, alkaline, formaldehyde-containing copper plating] solutions use d'toautocatalytically plate copper onto metals or non-metallic surfaces which comprises aerating such solutions with a gas containing elemental oxygen.
  • a solution for autocataly'tically plating copper which is stabilized against self-decomposition comprising an aqueous, alkaline solution of formaldehyde and a cupric ion which has been complexed so that the solution is free of cupric hydroxide, said solution containing a gas containing elemental oxygen.

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Description

grouping and R United States Patent PROCESS OF STABILIZING AUTOCATALYTIC COPPER PLATING SOLUTIONS Maynard C. Agens, Schenectady, N.Y., assignor to General Electric Company, a corporation of New York The present invention relates to a process for stabilizing copper plating solutions used to autacatalytiaclly plate copper onto metals or onto non-metallic surfaces. More particularly, this invention relates to a stabilization process which comprises producing oxidizing conditions within said plating solutions whereby the formation of cuprous oxide, which causes these solutions to become unstable, is greatly minimized or substantially prevented without the prevention of the reducing reaction which causes the copper to plate.
In my copending application S.N. 725,449, the copending applications of Robert M. Lukes, S.N. 725,450 and S.N. 725,452, all of which are filed concurrently herewith and assigned to the same assignee as the present invention, in the patent of A. E. Cahill et al., US. 2,874,- 072 and assigned to the same assignee as the present invention, and in the phamphlet Wein, Samuel, Copper Films, PB 111, 237, US. Department of Commerce, Oflice of Technical Services, 1953, there are disclosed plating solutions comprising aqueous, alkaline solutions containing formaldehyde and cupric ion complexed to prevent precipitation of cupric hydroxide to which my process is applicable.
Specifically, Cahill discloses complexing agents which are tartrates and salicylates used in the presence of carbonates all of which are water soluble. Lukes discloses in his application S.N. 725,450 complexing agents which are ethyleneaminoacetic acids which are selected from the class consisting of ethylenediaminetetraacetic acid, diethylenetriaminepentaacetic acid and 1,2-cyclohexylenediaminetetraacetic acid. In application S.N. 725,452,
Lukes discloses complexing agents corresponding to the formula:
$I CHzCH-OH),,
om-o 0 on where m and n are both integers and are at least 1 and not more than 2, p is an integer and is at least 0 and not more than 1, the sum of m, n and p equaling 3;.R is a member of the group consisting of hydrocarbon radicals having from 1 to carbon atoms, and the is a member of the group consisting of hydrogen and methyl. In my copending application I disclose complexing agents which correspond to the formula:
BI Cardin-0H "ice where R is a hydrocarbon radical having from 1 to 10 carbon atoms and, in addition, when p=0 and n=1, R also represents the R! CHr-H-OH CH2CH2-N GHa-(fH-OH RI grouping. R is a substituent selected from the group consisting of hydrogen and methyl, m is an integer and is at least 1 and no more than 4, n is an integer and is at least 0 and no more than 3, p is an integer and is at least 0 and not more than 1. The particular values of m, n, and p must be so chosen that they fulfill the following equation: +p
Further details concerning the use of these solutions are shown by the examples and by reference to the Cahill patent and the above-mentioned copending applications.
Many of the solutions disclosed in the Wein publication can form copper films or mirrors on surfaces that have not been sensitized with metallic films.
All of these solutions autocatalytically plate copper. By this terminology I mean that the solutions are capable of plating copper without the application of an external force, e.g., electricity. 7
Solutions known to autogenously plate copper as a smooth, adherent coating do so according to the following equation:
A subordinate and yet significant, reaction also occurs as illustrated by the following equation:
Since the reaction expressed by Equation II does not require activation by an extraneous material, it will occur merely upon the solution standing at room temperature and is hastened by heating. The cuprous oxide product is reduced by the alkaline formaldehyde solution to copper metal which is one of the metals that is catalytically active in initiating the plating reaction expressed by Equation 1. Therefore, the reaction of Equation Ilcauses these solutions to spontaneously decompose and'to become useless upon standing for long periods. j Although the complexing agents used in any of the above copending applications greatly suppress the reaction expressed by Equation 11, nevertheless, high concentrations of cupric ion andthe high alkalinity of the solutions over-ride some of the efiect of these complexing agents. Furthermore, it is not possible to completely suppress Equation H with any complexing agent.
Therefore, all of the solutions used to autocatalytically plate copper, such as those described in the above-identified applications have a finite life, that would be very desirable to extend. I have now found a very simple and easy method for performing this function. My invention comprises aerating these solutions with an oxygen'containing gas during storage or other periods of nonuse, and also while it is being used to plate copper. Aeration can be accomplish with pure oxygen or oxygen diluted with any inert gas such as argon, neon, krypton, nitrogen, and the like,'the simplest gaseous mixture to use being air itself even though it does contain a minor amount of carbon dioxide which reacts with the alkali in the solution. From what I can determine by experiment, the effect of oxygen is to either prevent the formation of cuprous oxide or to reoxidize the cuprous oxide back to soluble cupric compounds so quickly that no noticeable oir will usually be required. .A'filter i 3 precipitate can be observed. This is based on my observations that the plating solutions remain clear and free of any precipitate for extended periods of time providing a. gasv containing elemental oxygen, more commonly re ferredcto as an oxygen-containing gas, is blowing through the solutions. If I stop the flow of gas, a precipitate will form in time which will disappear almost as soon as I start aerating again. However, if I delay the start-up of the gas stream for a period long enough that the cuprous oxide is converted to copper, the copper will not dissolve. To restore stability in this case, the copper must be removed from contact with the solution, for example by filtration, centrifugation, decantation, etc. Furthermore, I have found that best results are obtained Ijhave the gas dispersed a s'very fine bubbles which areuuniformly distributed throughout the entire solution. Should, I fail to do this, I have noticed'that precipitation will occur in those-portions of the'solution not contacted by the gas, stream. Immediate correction of this condition can be effected by vigorous agitation. I have found that the best method of carrying my invention into effect is 'tointroduce the oxygen containing gas stream through a disperser such as a fritted glass disk or a po-' rous. ceramic disk so that the gas is. broken up into very fine bubbles, and to use vigorous agitation to insure that these bubbles are distributed throughout'the entire volume of the plating, solution. Sinceall metals that are notattacked by the alkaline. solutions. are catalytically active with the plating solution, the gas inlet and disperser must'be non-metals. Alternatively, of course, more than one stream of gas can be introduced into the solution; Providing the gas inlets are properly placed, and the volume oftheincoming gas is sufiicient, no further agitation is required since the gas streams themselves will provide suflicient agitation of the solution. Preferably, the entire liquid phase should be saturated with theoxygencontaining gas at all times. Filters can be used in conjunction with the aeration to' remove any solid material. Superatmospher-ic gas pressure can be'used but is notrequired. Sub-atmospheric pressure is not desirable since it does not permit as elfective saturation of the solution with the oxygen-containinggas as do higher pressures. 1
. I have also found that aeration can be accomplished by flowing thin films of the plating solutions over the surfaces to be plated. By this means, a small volume of l-iquidis exposed to a large volume of oxygen-containing gas. .By inclining the surfaces so that the liquid flows rapidly, agitation is also provided. The surfaces to be plated can be arranged in a stepwise fashion so that the liquid cascades from one surface to the nextinseries. If non-metallic'spray equipment is used, the plating solu tion can be sprayed as'anatomized 'm'istv to provide aera tion. In anyof these applications, if a reservoir ofliquid is present, additional. aeration of the liquid in the rese'r can; also be installed 1 1112118 line to remove any solid material; 1
Since theamount of oxygen actually consumed is extremely small, there is no critical concentration of oxy-- gen required in the gas composition used in my process. The'actual amount of oxygen is dependent on the cupric ionooncentration. This amount can be supplied by low oxygen concentration at fast flow rates or highconcem tration at low flow rates. From a practical standpoint,- there is no advantage in using a gas containing less oxygen than the approximately 20% contained in air, since this is the cheapest and most readily available oxygen-containing gas. Oxygen in a compressed gas cyclinder is a convenient source to use where there is no source of compressed air, or where mobility of the plating equipment is desired; However, my results with pure oxygen have shown no added benefits over the results I obtain with The oxygen-containing gas should be free of oils,
greases and. other contaminants that would afiect'the quality of the .copper'plate produced by the solutions;
Preferably, the container for the plating solutions should s r am 4 be 9 arreassd a he e t gases o n t a -T a ma t than the amount of reagents. In this regard, some loss of formaldehyde will always occur, due to its volatilization in the gas stream. This loss can be compensated for by additions of aqueous formaldehyde continuously or at prescribed intervals so as to maintain the concentration required to produce the plating reaction. In order, that those skilled in the art may understand how my invention can be carried into eifect, the following examples are given by way of illustration, and not by way of limitation.
Example 1 One liter of a plating solution was made by dissolving the following ingredients in enough water to make one liter of solution:
Aqueous 37% formaldehyde,.25 m1.
Theabove solution was divided into. two portions; one portion was used asa control and was allowed to standat room'temperature without any further treatment. The other portion was aerated by introduction of 'air into: the solution through a fritted glass disk. It was not mechanically stirred. At the end of approximately two hours, the control hadst'arfed'to decompose, as evidenced by the precipitationofi'copper. The aerated sample remained clear and unchanged. After leaving the solutions overnight; the control .sample had completely decomposed, as evidenced by the solution being colorless and all of the copper being a precipitate in the bottom of the'contain'er. The aerated sample still blue in color and had apH of 11.5,; There was a smali' amou'nt of copper metal pres.- entin the'solution indicatingrthat the solution 'had not been well stirred. The example was repeated, except that thistimethesolution was stirred vigorously in addition tobein'gfareated. At the endof "=12 hours, he decompoe sition of the plating solution had occurred, thepH was 119. A pieceof'sand-bl-asted paper-base, phenolic-resin laminatewas sensitized by immersing it for one minute in a stannous chloride solution 'made by dissolving l0 gra'rns of stannouschlon'de and 10 milliliters of 12 molar hydrochloricacid in one liter of water, rinsed with water, dipped for oneminute into. a' palladium chloride solution made by 'dissolvingdigram of palladium chloride and IOmillilite'rs of'l2- molar'hydrochloric' acid in one liter of water, andgagain rinsed in water. 'When the sensitized laminate was placed in the aerated solution, a coherent, bright film of copper plated onto the laminate simultaneously with the evolution of hydrogen from the surface.
Example 2 The solution as described in. Example 1 was duplicared d vid d im worortio n n p io a of nitrogen was adniitted atthe rate of 0.4 cubic foot per home; In the-second port-ion, a flow of pure en Wfl5 4mi s1 et-t a o 0-4 c t p hour. At the end of 1- 6; hours, thesolution aerated with the nitrogen was beginning to decompose and at the end of 2 /2 hours, was completely decomposed, as'evidenced by the solutionbeing colorless; The solution aerated with oxygen was still bright blue in color, with no signs of decomposition at the end of 48 hours, but there had been some depletion of formaldehyde. aldehyde; lost was replacedand, thepH adjusted to 128. When a piece of paper-base, phenolic-resin laminate which had beensensitized 'as in Examplel was placed in this solution, it was found that the'copper plated on the sensitized surface at a rate of'about 1 mil per hour. When 4 mils of copper had built, up 'on the board, it was removed from the solution. 7 The solution was aerated with oxygen for an additional 24 hours." When a sensitized piece of phenolic-resin laminate was inserted into the The amount of formplating solution, the copper deposited. at' the same fast rate of 1 mil per hour. After a film of 3 mils of copper had been plated onto the sample,.it was removed. Altogether, the solution hadremained clear and useful as a plating bath for about 80 hours with no signs of decomposition.
Example 3 Two liters of solution were prepared containing the following ingredients in the stated concentrations:
Molarity Cupric sulfate 0.10 Ethylenediaminetetraacetic acid 0.10 Potassium hydroxide 0.80 Formaldehyde 0.30
A piece of paper-base, phenolic-resin laminate having an area of 50 sq. inches which had been sensitized with palladium as in Example '1 was placed in this solution. Air was bubbled in through a fritted glass filter diifuser at the rate of 0.2 liter per minute, while the solution was stirred vigorously with a mechanical stirrer. At the end of 5 hours an additional 25'milliliters of formaldehyde was added and 2 milliliters of a wetting agent comprising an ethylene oxide and propylene oxide polymer was added. The thickness of the copper coating was 0.6 to 0.7 mil thick and no decomposition of the plating solution had occurred. At the end of an additional 1 /2 hours, the solution was plating satisfactorily and was left overnight, for 15 hours. No decomposition of the solution occurred during this time and the solution was still plating, however, at a very slow rate. An additional 50 milliliters of formaldehyde was added and enough potassium hydroxide was added to increase the initial molarity of the base by an additional 0.80. This caused the solution to start plating rapidly again. At the end of 4 /2 hours, the solution was still plating at a rate of about 0.1 mil per hour and the total thickness of the copper plate was about 2 /2 mils. Although no undesirable decomposition of the solution occurred, the plating reaction was stopped at this point by acidifying the solution to a pH of 2, whereby 56 of the original 60 grams of the ethylenediaminetetraacetic acid was recovered by filtration of the solution, since this reagent is insoluble in the reaction mixture at this pH.
Example 4 One liter of solution was made containing the following ingredients:
Grams Cupric nitrate trihydrate 15 Sodium hydroxide 20 Sodium bicarbonate Sodium potassium tartrate 30 This solution was divided into four equal portions of 250 milliliters each, and into each portion 25 milliliters of 37% aqueous formaldehyde was added. One portion was left standing at room temperature as a blank; the second portion was aerated with air using a fritted glass disk to disperse the gas stream. A paper-base, phenolicresin laminate which had been sensitized as in Example 1 was placed in each of the third and fourth portions. The third portion was not aerated and the fourth portion was aerated in the same way as the second portion. In both the third and fourth solutions, the seeded board was plated rapidly with copper. At the end of about 20 minutes, both the first and third solutions which had not been aerated, were starting to decompose as was evidenced by the formation of precipitate of cup'rous oxide. Both the second and fourth solutions were still clear, with no evidence of decomposition at the end of 7 hours.
Example 5 A plating composition comprising three solutions useful in making copper mirrors was made up as follows.
Solution A:
Cupric sulfate pentahydrate ..g 20 Glycerol ml Aqueous ammonia (28%) ml 20 Solution B: p p
' Sodium hydroxide (9% aqueous sol.) ml 400 Sucrose (10% aqueous sol.) ml 200 m1... 0.5 Water ml 250 Solution C:
Aqueous formaldehyde (37%) ml 80 Water ml 1250 The three solutions combined in the proportion Solution A ml Solution B ml 850 Solution C ml 1330 The resulting plating solution was divided into two portions. One portion was aerated with air at the rate of 0.5 cubic foot per hour while the other portion was permitted to stand at ambient temperature as a control. When a piece of paper base-phenolic-resin laminate that had been sensitized with palladium as in Example 1 was placed in each of the two portions copper plated onto the sensitized area. The pieces of laminate were removed and the solutions allowed to stand overnight. In the morning the non-aerated sample had formed a smooth mirror over the entire area of the glass beaker contacted by the solution which was now depleted of copper. No sensitization of the non-metallic (glass) surface is necessary with this solution to obtain the mirror. The aerated sample had not decomposed either by forming a copper mirror or by precipitating cuprous oxide. At the end of three days it was still stable and plated copper on the sensitized laminate. By stopping the aeration of a sample of this solution, a copper mirror will form on the walls of the container on standing overnight.
7 Example 6 One liter of solution was made containing the following concentration of ingredients:
Molarity Cupric sulfate 0.1 Glycerol 0.45 Ammonium hydroxide 0.4 Sodium hydroxide 0.6
Formaldehyde (37% aqueous sol.), 80 ml.
Example 7 One liter of solution was made containing the follow ing ingredients in the stated concentration:
Molarity Cupric sulfate 0.1 Glycerol 0.45 Sucrose .15 Ammonium hydroxide 0.4 Sodium hydroxide 0.4
Aqueous formaldehyde (37%), 80 ml.
The procedure of Example 6 was repeated with almost identical results. The test for the aerated sample was discontinued at the end of eight hours with no sign of decomposition.
Example 8 In order to obtain some explanation as to the function of oxygen in preventing the decomposition of these platr 7 ing solutions, a solution was made up containing the following ingredients in the stated concentrations:
. I a r Molarity Ethylenediaminetetraacctic acid 0.10 Potassium hydroxide 0.60
into this solution, 0.05 mole of-:cuprous oxide was added, mechanical agitation was, supplied, and air at the 1 The following example was carried out to see whether I or not aeration'could stop decomposition. once it had been initiated. One liter of solution was made up containing the following ingredientsi Grams Cupric sulfate pentahydrate 25 Ethylenediaminetetraacetic acid 60 Sodium hydroxide 52 Twenty-two milliliters of 37% aqueous formaldehyde solution was added to 875 milliliters of the above solution, which was agitated with a mechanical stirrer and aerated with oxygen at the rate of 0.4 cubic foot per hour. A
sample of this solution showed a light transmission of 98 /2 when measured in a spectrophotometer using lightof a wavelength of 450 millimicrons. The mechanical stirrer was shut off and the stream of oxygen stopped. At the end of approximately 1 hour, the solution became turbid, indicating that it was starting to decompose. At
c this point, the light transmission was found to .have
dropped to approximately 2%, n The stream of oxygen and the stirring were againstarted, which immediately caused the turbidity to disappear. After 15 minutes of aeration, a sample was taken and it was found that the light transmission had increasedto 90%. During the entire experiment the pH of the solution had remained at 12.8. This example shows that aeration with an oxygen- 7 containing gas can stop deednipositienof these plating solutions if initiated in the early stages'of the, decomposition. i
As illustrated by the above examples, my method of stabilization is applicable to all plating solutions which are based on the reactionof formaldehyde. with a cupric salt complex in an alkaline solution :to. producea film of' copper metal. Thisrstabilizationv is apparently caused by the abilitylof the oxygen-containing gas to prevent the precipitation or, formation ofic'uprous oxide by thefsec ondary reaction outlined above.
The above examples haveillustrated many o'f the modifications and variations of the present invention, but obviously, other modifications and variations are possible in light of the above teaching. For example, the plating solutions aerated according to my invention can be used at higher temperatures than the non-aerated plating solutions. It is therefore to be understood thatchanges'may be made in the particular embodiments of. the invention described which are within the full intended scope of'the invention as defined by the appended claims.
What I claim as new and desire to secure byLetters Patentof the United States is:
1. The process for stabilizing aqueous, alkaline, formaldehyde-containing copper plating] solutions use d'toautocatalytically plate copper onto metals or non-metallic surfaces which comprises aerating such solutions with a gas containing elemental oxygen.
.2. The process of claim 1 wherein the gas is air.
3. The process of claim 1 wherein the-gas is substantially pure oxygen.
4. The process of claim 1 wherein the plating solutions are saturated with the gas. i
v 5. The process of claim 1 wherein aeration is used in conjunction with mechanical'agitation.
6. The process of claim 1 wherein the gas is dispersed throughout the entire volume of plating solution.
7. A solution for autocataly'tically plating copper which is stabilized against self-decomposition comprising an aqueous, alkaline solution of formaldehyde and a cupric ion which has been complexed so that the solution is free of cupric hydroxide, said solution containing a gas containing elemental oxygen.
8. The solution of claim.7 wherein the gas is air.
9. The solution of claim 7 wherein the gas is substantially pure oxygen. a
10. The solution of claim 7 wherein the solution is saturated with the gas.
References Cited in the file of this patent Owen Aug. 6, 1957

Claims (1)

  1. 7. A SOLUTION OF AUTOCATALYTICALLY PLATING COPPER WHICH IS STABILIZED AGAINST SELF-DECOMPOSITION COMPRISING AN AQUEOUS, ALKALINE SOLUTION OF FORMALDEHYDE AND A CUPRIC ION WHICH HAS BEEN COMPLEXED SO THAT THE SOLUTION IS FREE OF CUPRIC HYDROXIDE, SAID SOLUTION CONTAINING A GAS CONTAINING ELEMENTAL OXYGEN.
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Cited By (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2996408A (en) * 1958-03-31 1961-08-15 Gen Electric Copper plating process and solution
US3095309A (en) * 1960-05-03 1963-06-25 Day Company Electroless copper plating
US3222207A (en) * 1961-10-06 1965-12-07 Ibm Process of producing metallic deposits
US3257215A (en) * 1963-06-18 1966-06-21 Day Company Electroless copper plating
US3261711A (en) * 1962-12-17 1966-07-19 Honeywell Inc Electroless plating
US3269861A (en) * 1963-06-21 1966-08-30 Day Company Method for electroless copper plating
US3281266A (en) * 1963-04-12 1966-10-25 Honeywell Inc Electroless plating
US3300335A (en) * 1963-11-20 1967-01-24 Dow Chemical Co Electroless metal plating with foam
US3307972A (en) * 1963-03-11 1967-03-07 Bell Telephone Labor Inc Electroless copper deposition
US3318711A (en) * 1964-04-02 1967-05-09 Sel Rex Corp Immersion plating process for the deposition of copper
US3326700A (en) * 1963-06-12 1967-06-20 Rudolph J Zeblisky Electroless copper plating
US3329512A (en) * 1966-04-04 1967-07-04 Shipley Co Chemical deposition of copper and solutions therefor
DE1248419B (en) * 1964-08-17 1967-08-24 Collardin Gmbh Gerhard Immersion bath for the electroless deposition of copper-tin layers
US3340164A (en) * 1963-12-26 1967-09-05 Sperry Rand Corp Method of copper plating anodized aluminum
US3361580A (en) * 1963-06-18 1968-01-02 Day Company Electroless copper plating
US3382079A (en) * 1964-12-16 1968-05-07 Ibm Electroless ni-fe deposition process
DE1300762B (en) * 1965-03-23 1969-08-07 W Kampschulte & Cie Dr Alkaline solution and process for depositing copper on non-conductors
US3770464A (en) * 1971-10-12 1973-11-06 Shipley Co Dry replenishment of electroless copper solutions
US3793038A (en) * 1973-01-02 1974-02-19 Crown City Plating Co Process for electroless plating
US4138267A (en) * 1976-12-28 1979-02-06 Okuno Chemical Industry Company, Limited Compositions for chemical copper plating
US4152467A (en) * 1978-03-10 1979-05-01 International Business Machines Corporation Electroless copper plating process with dissolved oxygen maintained in bath
US4167601A (en) * 1976-11-15 1979-09-11 Western Electric Company, Inc. Method of depositing a stress-free electroless copper deposit
US4228213A (en) * 1979-08-13 1980-10-14 Western Electric Company, Inc. Method of depositing a stress-free electroless copper deposit
US4431685A (en) * 1982-07-02 1984-02-14 International Business Machines Corporation Decreasing plated metal defects
US4534797A (en) * 1984-01-03 1985-08-13 International Business Machines Corporation Method for providing an electroless copper plating bath in the take mode
US4550036A (en) * 1984-10-18 1985-10-29 Hughes Aircraft Company Electroless silver plating process and system
US4632852A (en) * 1984-06-18 1986-12-30 Hitachi, Ltd. Process for electroless copper plating
US4639380A (en) * 1985-05-06 1987-01-27 International Business Machines Corporation Process for preparing a substrate for subsequent electroless deposition of a metal
US4654126A (en) * 1985-10-07 1987-03-31 International Business Machines Corporation Process for determining the plating activity of an electroless plating bath
US4720404A (en) * 1984-02-04 1988-01-19 Josif Culjkovic Aqueous alkaline bath for the chemical deposition of copper, nickel, cobalt and their alloys
US4853320A (en) * 1987-09-16 1989-08-01 U.S. Philips Corporation Method of locally providing metal on a surface of a substrate
US4865888A (en) * 1987-06-16 1989-09-12 Hitachi, Ltd. Process for electroless copper plating and apparatus used therefor
US4904506A (en) * 1986-01-03 1990-02-27 International Business Machines Corporation Copper deposition from electroless plating bath
US4967690A (en) * 1986-02-10 1990-11-06 International Business Machines Corporation Electroless plating with bi-level control of dissolved oxygen, with specific location of chemical maintenance means
EP0236718B1 (en) * 1986-02-10 1991-05-08 International Business Machines Corporation Electroless plating with bi-level control of dissolved oxygen
US5318803A (en) * 1990-11-13 1994-06-07 International Business Machines Corporation Conditioning of a substrate for electroless plating thereon
US6065424A (en) * 1995-12-19 2000-05-23 Cornell Research Foundation, Inc. Electroless deposition of metal films with spray processor
US20090253262A1 (en) * 2005-10-14 2009-10-08 Blue29, Llc Electroless plating system
EP2672520A1 (en) 2012-06-06 2013-12-11 SEMIKRON Elektronik GmbH & Co. KG Method for electroless deposition of a copper layer, electroless deposited copper layer and semiconductor component comprising said electroless deposited copper layer

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US2759845A (en) * 1954-10-25 1956-08-21 Metropolitan Mirror And Glass Processes of precipitating copper from copper sulfate solutions and precipitating media for so doing
US2801935A (en) * 1953-09-30 1957-08-06 Merck & Co Inc The use of hydrazine tartrate salts in the chemical deposition of metals

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US2801935A (en) * 1953-09-30 1957-08-06 Merck & Co Inc The use of hydrazine tartrate salts in the chemical deposition of metals
US2759845A (en) * 1954-10-25 1956-08-21 Metropolitan Mirror And Glass Processes of precipitating copper from copper sulfate solutions and precipitating media for so doing

Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2996408A (en) * 1958-03-31 1961-08-15 Gen Electric Copper plating process and solution
US3095309A (en) * 1960-05-03 1963-06-25 Day Company Electroless copper plating
US3222207A (en) * 1961-10-06 1965-12-07 Ibm Process of producing metallic deposits
US3261711A (en) * 1962-12-17 1966-07-19 Honeywell Inc Electroless plating
US3307972A (en) * 1963-03-11 1967-03-07 Bell Telephone Labor Inc Electroless copper deposition
US3281266A (en) * 1963-04-12 1966-10-25 Honeywell Inc Electroless plating
US3326700A (en) * 1963-06-12 1967-06-20 Rudolph J Zeblisky Electroless copper plating
US3257215A (en) * 1963-06-18 1966-06-21 Day Company Electroless copper plating
US3361580A (en) * 1963-06-18 1968-01-02 Day Company Electroless copper plating
US3269861A (en) * 1963-06-21 1966-08-30 Day Company Method for electroless copper plating
US3300335A (en) * 1963-11-20 1967-01-24 Dow Chemical Co Electroless metal plating with foam
US3340164A (en) * 1963-12-26 1967-09-05 Sperry Rand Corp Method of copper plating anodized aluminum
US3318711A (en) * 1964-04-02 1967-05-09 Sel Rex Corp Immersion plating process for the deposition of copper
DE1248419B (en) * 1964-08-17 1967-08-24 Collardin Gmbh Gerhard Immersion bath for the electroless deposition of copper-tin layers
US3382079A (en) * 1964-12-16 1968-05-07 Ibm Electroless ni-fe deposition process
DE1300762B (en) * 1965-03-23 1969-08-07 W Kampschulte & Cie Dr Alkaline solution and process for depositing copper on non-conductors
US3329512A (en) * 1966-04-04 1967-07-04 Shipley Co Chemical deposition of copper and solutions therefor
US3770464A (en) * 1971-10-12 1973-11-06 Shipley Co Dry replenishment of electroless copper solutions
US3793038A (en) * 1973-01-02 1974-02-19 Crown City Plating Co Process for electroless plating
US4167601A (en) * 1976-11-15 1979-09-11 Western Electric Company, Inc. Method of depositing a stress-free electroless copper deposit
US4138267A (en) * 1976-12-28 1979-02-06 Okuno Chemical Industry Company, Limited Compositions for chemical copper plating
US4152467A (en) * 1978-03-10 1979-05-01 International Business Machines Corporation Electroless copper plating process with dissolved oxygen maintained in bath
US4228213A (en) * 1979-08-13 1980-10-14 Western Electric Company, Inc. Method of depositing a stress-free electroless copper deposit
US4431685A (en) * 1982-07-02 1984-02-14 International Business Machines Corporation Decreasing plated metal defects
US4534797A (en) * 1984-01-03 1985-08-13 International Business Machines Corporation Method for providing an electroless copper plating bath in the take mode
US4720404A (en) * 1984-02-04 1988-01-19 Josif Culjkovic Aqueous alkaline bath for the chemical deposition of copper, nickel, cobalt and their alloys
US4632852A (en) * 1984-06-18 1986-12-30 Hitachi, Ltd. Process for electroless copper plating
US4550036A (en) * 1984-10-18 1985-10-29 Hughes Aircraft Company Electroless silver plating process and system
US4639380A (en) * 1985-05-06 1987-01-27 International Business Machines Corporation Process for preparing a substrate for subsequent electroless deposition of a metal
US4654126A (en) * 1985-10-07 1987-03-31 International Business Machines Corporation Process for determining the plating activity of an electroless plating bath
US4904506A (en) * 1986-01-03 1990-02-27 International Business Machines Corporation Copper deposition from electroless plating bath
EP0236718B1 (en) * 1986-02-10 1991-05-08 International Business Machines Corporation Electroless plating with bi-level control of dissolved oxygen
US4967690A (en) * 1986-02-10 1990-11-06 International Business Machines Corporation Electroless plating with bi-level control of dissolved oxygen, with specific location of chemical maintenance means
US4865888A (en) * 1987-06-16 1989-09-12 Hitachi, Ltd. Process for electroless copper plating and apparatus used therefor
US4853320A (en) * 1987-09-16 1989-08-01 U.S. Philips Corporation Method of locally providing metal on a surface of a substrate
US5318803A (en) * 1990-11-13 1994-06-07 International Business Machines Corporation Conditioning of a substrate for electroless plating thereon
US6065424A (en) * 1995-12-19 2000-05-23 Cornell Research Foundation, Inc. Electroless deposition of metal films with spray processor
US20090253262A1 (en) * 2005-10-14 2009-10-08 Blue29, Llc Electroless plating system
US7972652B2 (en) * 2005-10-14 2011-07-05 Lam Research Corporation Electroless plating system
EP2672520A1 (en) 2012-06-06 2013-12-11 SEMIKRON Elektronik GmbH & Co. KG Method for electroless deposition of a copper layer, electroless deposited copper layer and semiconductor component comprising said electroless deposited copper layer

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