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Publication numberUS2987453 A
Publication typeGrant
Publication dateJun 6, 1961
Filing dateApr 14, 1959
Priority dateApr 14, 1959
Publication numberUS 2987453 A, US 2987453A, US-A-2987453, US2987453 A, US2987453A
InventorsDu Rose Arthur H
Original AssigneeHarshaw Chem Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of electrodepositing chromium
US 2987453 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

June 6, 1961 A. H. DU ROSE METHOD OF ELECTRODEPOSITING CHROMIUM Filed April 14, 1959 A. H. DU ROSE. INVENTOR.

Patented June 6, 1961 2,987,453 NIETHOD F ELECTRODEPOSITING CHROMIUM Arthur H. Du Rose, Euclid, Ohio, assignor to The Harshaw Chemical Company, Cleveland, Ohio, a corporation of Ohio Filed Apr. 14, 1959, Ser. No. 806,330 3 'Claims. (Cl. 204-51) This invention relates to titanium anodes having platinum coatings thereon.

Platinum coated titanium anodes are known to the art. However, in the field of electroplating, platinum coated titanium anodes have been found suitable only for nickel plating in the related fields of nickel and chrome plating processes. Whereas the platinum coated titanium anodes employed in nickel plating solutions were found to be relatively stable towards dislodgement of the platinum coating, such anodes when employed in chrome plating solutions were found to have coating particle dislodging tendencies which removed the platinum and in a short time stopped the anodic current. It further appears that none ofthe workers in the field of platinum coated anodes have attempted to improve the efliciency of the anode by confining the area of effective current to that area in the immediate proximity of the object being plated.

It is, therefore, an object of this invention to produce an insoluble anode which is suitable for both nickel and chrome plating processes.

It is another object of this invention to produce a titanium anode with an adherent platinum coating.

It is still another object of this invention to produce an insoluble anode having an effective current carrying surface only in the area of the object being plated.

Of the many problems which have faced the electroplating industry, the selection of an insoluble anode suitable for both nickel and chrome plating has been one of the most perplexing. Anodes of the insoluble type have been found to be subject to particle dislodging tendencies. The problem presented by particle dislodgment is increased when the insoluble anode is used in more than one type of bath, such as for instance, in both nickel and chrome plating baths.

Another problem which faces the electroplating industry is that of obtaining a coating having uniform thickness. The problem of non-uniformity in coating thickness is especially apparent when the object being coated has recessed areas. It has been found that these recessed areas receive less current and, therefore, obtain a lesser deposit of metal from the plating solution. Each plating solution is found to have its peculiarities in the degree to which irregularity of the surface of the object being coated will affect the uniformity of the coating. The peculiarity of each individual plating solution may be defined in terms of throwing power. Throwing power refers to the uniformity of plate thickness that can be expected on a shaped article over the surface of which the current density will vary. The dis tribution of the plating current is influenced by the relative distance of any given part of the surface from the anodes. No plating bath has a throwing power great enough to produce a uniform plate thickness on complex shaped cathodes.

Because of the low throwing power of nickel and chrome plating compositions, auxiliary anodes such as auxiliary anodes of the conforming type, have been found to be desirable when plating objects having irregular surfaces. It can, therefore, be seen that an insoluble anode which will function as an auxiliary anode free from particle dislodging tendencies in both nickel and chrome plating solutions would be a tremendous advance in the electroplating industry. The platinum coated titanium anode produced by the process of this invention has been found to answer these problems.

The insoluble anodes of the prior art are lead, carbon and platinum coated titanium anodes. While platinum coated titanium of the prior art is suitable for nickel plating, it has been found to be subject to the same particle dislodging tendencies in chrome plating solutions which lead and carbon anodes exhibit in both nickel and chrome plating solutions. I have now discovered a process whereby the dislodging tendencies of platinum coated titanium insoluble electrodes in a chrome plating bath is eliminated, thereby producing an auxiliary anode which will function satisfactorily in both nickel and chrome plating baths.

Titanium in itself is not a suitable anode material because the protective oxide film which forms on its surface resists the passage of an anodic electric current. Research has shown, however, that this high resistivity is very much reduced when titanium is brought into electrical contact with a second metal such as platinum. Platinum, deposited as a thin film on the titanium, either in sheet or rod form, produces a conductive surface suitable for an anode. I have found that a platinum coating which does not exhibit dislodging tendencies in a chrome plating bath may be produced when the platinum is plated on titanium wire and then heated from 400 C. to 800 C. for 15 seconds or longer. A special type of atmosphere is not required for this heating operation. A wire anode produced in this manner will function indefi nitely in a chrome solution.

It appears that the platinum becomes bonded to the titanium by means of heat induced interdilfusion of platinum with the titanium base metal. The interdiffused layer serves to firmly anchor the pure platinum external coat to the pure titanium base. The interdiffused bonding also serves to prevent the sludging of the platinum coating which rendered the platinum coated electrodes of the prior art useless in chrome plating baths.

The following treating cycle for a titanium base in sheet or rod form has been found to be desirable in the process of this invention:

(1) Descale by 15 seconds to 2 minutes immersion in equal parts by volume of 48% HF, nitric acid and water.

(2) Rinse in water.

(3) Immerse in alkaline cleaning solution.

(4) Rinse.

(5) Dip in 45% HBF at a temperature from F. to F.

(6) Rapid rinse.

(7) Plate at 2-30 amperes per square foot in a highly acid platinum plating solution. The thickness used is on the order of 0.030.2 mil.

(8) Heat at 400 C. to 800 C. for 15 seconds to 1 hour. An inert or reducing atmosphere is not necessary.

In some cases a portion (say 50%) of the final platinum thickness was first applied and heat treated and then the remainder of the platinum deposited. This procedure was advantageous when the initial platinum,

coating tended to be powdery or of poor quality. The second coating was also heat treated when the plural coating procedure was applied. If the initially deposited coating appeared good, there was no advantage in applying the plural coating procedure.

Three types of platinum plating solutions weer used:

(1) A platinum chloride solution containing 6 g./l. Pt and 300 cc./l. of hydrochloric acid.

(2) A platinum chloride solution containing 6 g./l. Pt and 300 cc./1. of phosphoric acid.

(3) A proprietary solution (Platinex) containing 12 g./l. of Pt.

The latter solution produced by far the better deposits. They were all used at 150 F. to 175 F.

As insoluble auxiliary anodes generally have the same area presented toward the workpiece, uniform current density over the entire surface of the anode is not required. An extremely effective anode has been produced by the process of this invention by coating a single area or face of the auxiliary titanium anode, thereby limiting the area coated with platinum while increasing the eifective current being utilized. An insulating coating need not be placed on the areas of the titanium anode which are free of platinum as titanium will form an oxide layer which is in itself a good insulator. The anode is also greatly reduced in cost by eliminating unnecessary platinum coating.

The accompanying drawing further illustrates the various embodiments of the invention:

The single figure, which is not to scale, represents a perspective view of the novel auxiliary anode disposed in a plating assembly. The assembly consists of a rack holder 1, holding two recessed objects to be plated 2 and 2; said recessed objects 2 and 2' having their recessed areas located at 3 and 3' respectively. The auxiliary anode 4 is coupled to the rack holder 1 by means of insulated coupling members 6 and 6. The auxiliary anode 4 is composed of a titanium Wire base having a platinum coated portions, greatly exaggerated for purposes of illustration, disposed on the areas 5 and 5' and having a suitable electrical contact clip 7 disposed at its upper extremity.

In use the rack holder 1 is hung on the cathode bar of an electroplating tank, whereby the rack holder becomes conductive and causes the objects to be plated 5 and 5' to become cathodic to the primary anodes disposed in the electroplating tank. The auxiliary anode 4 is attached to the anode rail of the electroplating tank by means of the electrical contact clip 7. The objects to be plated-5 and 5 are thereby subjected to anodic current from both the primary anode and the auxiliary anode 4. The current flowing from the auxiliary anode 4 flows from the platinum coated areas 5 and 5, thereby subjecting the recessed portions 3 and 3' of the objects 2 and 2' to an increased current density. The result of the increased current density in these recessed portions is to produce more uniform 4 coating over the entire surface area of the plated objects. Without the auxiliary anode the thickness of the edge portions of the objects 2 and 2' might be at least five times as great as that in the areas 3 and 3.

The assembly of this invention may be used for nickel plating an object and then without breaking down the assembly, the entire structure may be removed with suitable washing operations to a chrome plating bath. The novel platinum coated electrode of this invention makes possible the removal of the assembly from one tank to another, the platinum coated titanium anode of this invention being free from particle dislodging tendencies in either nickel or chrome plating baths.

Having thus described my invention, what I claim is:

1. The method of electrodepositing chromium, including the steps of suspending the object to be plated in a chromium plating bath employing a platinum coated titanium auxiliary anode, said auxiliary anode being prepared by electroplating a platinum coating on a titanium base and then heat treating the coated base at a temperature of 400 C. to 800 C.

2. The method of claim 1 wherein said platinum coating is applied by plural applications, each application being subjected to said heat treating operation.

3. The method of electrodepositing chromium, including the step of suspending the object to be plated in a chromium plating bath employing a titanium auxiliary anode having a discontinuous coating thereon; the object to be plated being disposed so as to be in the immediate proximity of the platinum plated portions of the auxiliary anode, said auxiliary anode being prepared by discontinuously plating a platinum coating on a titanium base and then heat treating it at a temperature of from 400 C. to 800 C.

References Cited in the file of this patent UNITED STATES PATENTS 2,719,797 Rosenblatt Oct. 4, 1955 2,798,843 Slomin et a1 July 9, 1957 2,834,101 Boam et al. May 13, 1958 OTHER REFERENCES Cotton: Platinum Metals Review, vol. 2, April 1958, pages 45 to 47.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2719797 *May 23, 1950Oct 4, 1955Baker & Co IncPlatinizing tantalum
US2798843 *Oct 29, 1953Jul 9, 1957Rohr Aircraft CorpPlating and brazing titanium
US2834101 *Feb 23, 1955May 13, 1958Curtiss Wright CorpMethod of brazing titanium
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3055811 *May 8, 1961Sep 25, 1962Universal Oil Prod CoElectrolysis with improved platinum plated titanium anode and manufacture thereof
US3177131 *Aug 12, 1963Apr 6, 1965Ici LtdMethod for the production of platinum coated titanium anodes
US3247083 *Apr 1, 1964Apr 19, 1966Raymond Louis WMethod of chromium electrodeposition
US3250691 *May 28, 1962May 10, 1966Pittsburgh Plate Glass CoElectrolytic process of decomposing an alkali metal chloride
US3254015 *Jul 28, 1961May 31, 1966Bishop & Co Platinum Works JProcess for treating platinum-coated electrodes
US3271289 *Oct 10, 1963Sep 6, 1966Oronzio De Nora ImpiantiMercury cathode electrolytic cell having an anode with high corrosionresistance and high electrical and heat conductivity
US3300396 *Nov 24, 1965Jan 24, 1967Walker Charles TElectroplating techniques and anode assemblies therefor
US3412000 *Apr 14, 1965Nov 19, 1968M & T Chemicals IncCathodic protection of titanium surfaces
US3864163 *Mar 24, 1972Feb 4, 1975Chemnor CorpMethod of making an electrode having a coating containing a platinum metal oxide thereon
US4052271 *Jun 25, 1976Oct 4, 1977Diamond Shamrock Technologies, S.A.Method of making an electrode having a coating containing a platinum metal oxide thereon
US4294670 *Oct 29, 1979Oct 13, 1981Raymond Louis WUsing consumable electrode
US5545310 *Mar 30, 1995Aug 13, 1996Silveri; Michael A.Method of inhibiting scale formation in spa halogen generator
US5676805 *Apr 16, 1996Oct 14, 1997BioquestSPA purification system
US5752282 *Mar 30, 1995May 19, 1998BioquestSpa fitting
US5759384 *May 13, 1996Jun 2, 1998BioquestWater purification system
US5885426 *Aug 26, 1997Mar 23, 1999BioquestSpa purification system
US6007693 *Mar 10, 1998Dec 28, 1999BioquestSpa halogen generator and method of operating
USRE28820 *Aug 5, 1975May 18, 1976Chemnor CorporationMethod of making an electrode having a coating containing a platinum metal oxide thereon
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Classifications
U.S. Classification205/284, 205/264, 204/288.3, 205/227, 204/290.14, 204/290.12, 204/288.6, 204/288
International ClassificationC25D17/10, C25D5/48, C25B11/00, C25B11/10, C25D5/50
Cooperative ClassificationC25D5/50, C25D17/10
European ClassificationC25D5/50, C25D17/10