US3924025A - Method of making an electrode having a coating of cobalt metatitanate thereon - Google Patents

Method of making an electrode having a coating of cobalt metatitanate thereon Download PDF

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US3924025A
US3924025A US384210A US38421073A US3924025A US 3924025 A US3924025 A US 3924025A US 384210 A US384210 A US 384210A US 38421073 A US38421073 A US 38421073A US 3924025 A US3924025 A US 3924025A
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cobalt
substrate
ruthenium
titanium
solution
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James M Kolb
Kevin J O'leary
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ELECTRODE Corp A DE CORP
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • C25B11/091Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds
    • C25B11/093Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds at least one noble metal or noble metal oxide and at least one non-noble metal oxide

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  • This electrode consists in general of a valve metal substrate bearing on its surface a valve metal oxideplatinum metal oxide solid solution-type coating. In such coatings, atoms of platinum metal are randomly substituted for atoms of valve metal in the characteristic rutile valve metal oxide crystal lattice.
  • Such electrodes exhibit remarkably low potentials when employed in a variety of electrolytic processes, e.g., as anodes for the production of chlorine by electrolysis of sodium chloride solutions.
  • a further advantage of such electrodes is that they exhibit a relatively low wearrate, that is, only a small amount of plantinum metal is consumed per ton of product manufactured.
  • Such electrodes are not entirely without disadvantage, however, in that owing to the amount of platinum metal required to be incorporated in the coating, the electrodes are expensive to fabricate.
  • the wear-rate is low, generally, for example, on the order of 0.10-0.15 gram of platinum metal per ton of chlorine produced, considering the tonnages involved a significant amount of platinum metal is irretrievably lost.
  • the electrodes become inactive. Hence, the cell must be disassembled for removal and replacement of the electrodes. For these reasons, the search for a coating material exhibiting all the advantages of the solid solutiontype coating, with the further advantage of a reduced wear-rate, continues.
  • a composition which is especially useful for application as an electrode coating, which composition consists essentially of a coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution.
  • a supporting substrate especially an electrically-conductive supporting substrate and particularly a valve metal substrate, an electrode is obtained which exhibits a low potential and which has extremely low platinum metal wear-rates.
  • the invention finds particular advantage when the coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution is applied to a valve metal base, the resulting structure being used as an anode for the production of chlorine by electrolysis of brine.
  • a reduction in the amount of platinum metal required per square foot of anode surface is possible, without sacrifree in the potential at which chlorine is discharged at the anode face.
  • the anode has a significantly lower platinum metal wear-rate per ton of chlorine produced.
  • a sample electrode has been prepared as is described more fully hereinbelow by application to a clean titanium substrate of a solution containing salts of titanium, ruthenium and cobalt.
  • the electrode exhibits re markable adhesion between the coating and the substrate.
  • Examination by X-ray diffraction indicates, in addition to the presence of the characteristic rutile Ti- O solid solution crystal structure, that there is also present crystalline cobalt metatitanate as a separate phase dispersed throughout the solid solution. It is apparent from the results obtained that the cobalt metatitanate in some manner stabilizes the solid solution, thus preventing normal wear to a great extent.
  • the metatitanate when subjected to X-ray diffraction analysis, must exhibit peaks characteristic of cobalt metatitanate. It is not necessary that the crystals be highly ordered, although this is preferred, only sufficiently so that discemable peaks are evidenced. While cobalt metatitanate having at least some degree of crystallinity is required and constitutes the invention in admixture with the solid solution, cobalt oxides and/or amorphous cobalt titanate may be present without substantial detriment. As is explained more fully hereinbelow, the extent of cobalt titanate crystallinity appears to depend upon the various heat treatments to which the electrode is subjected during preparation.
  • valve metal oxideplatinum metal oxide solid solutions By valve metal it is intended to refer to titanium, tantalum, zirconium and niobium, while by platinum metal the reference is to platinum, palladium, ruthenium, iridium, rhodium and osmium.
  • the quantities of the various ingredients of the composition of the present invention are conveniently expressed in terms of the mole ratios of the various metals present.
  • the ratio of valve metal to platinum metal plus cobalt should be within the range of 5: 1-1 :5 while the ratio of platinum metal to cobalt should be within the range of 4:1- 2:3.
  • a preferred range, especially when dealing with titanium, ruthenium and cobalt is, respectively, 10:2:3.
  • the crystalline cobalt metatitanate will constitute up to 35%, preferably 10-35%, still more preferably 25-35%, by weight, of the total solid solution plus crystalline cobalt 3 metatitanate.
  • compositions of the present invention will be as a coating applied to a conductive substrate.
  • the material itself absent a substrate, will find some application.
  • Techniques for preparation are in many respects standard to the preparation of solid solutions, with the additional inclusion of a cobalt compound. For example sealed tube or flame spray techniques may be applied.
  • the material thus obtained has a high degree of non-selective catalytic activity thus suggesting its use for the catalytic destruction of organic compounds, such as in exhaust emission.
  • the material may be impregnated into porous graphite for use as a fuel cell electrode or dispersed in an organic binder, such as a fluorocarbon binder, to prepare a porous electrode, again useful in fuel cells.
  • organic binder such as a fluorocarbon binder
  • the composition finds applica tion as a coating on a supporting substrate. Since the coating will not generally be sufficiently massive to conduct current from the primary souce, an electrically-conductive substrate will be employed. Additionally, the substrate will be one which, upon the possible mechanical failure of the applied coating, will be inert to the environment in which it is employed. Preferably, at least when use is to be as an anode for the production of chlorine, the substrate will be a valve metal, typically titanium.
  • the physical configuration of the supporting substrate is independent of the present invention and depends primarily upon the cell design in which the electrode is to be employed.
  • a protective or barrier layer to achieve a desired chemical or physical effect, for example, a manganese dioxide layer serving to prevent the diffusion of oxygen through the coating to the underlying substrate.
  • protective ceramic layers may be applied over the coating, as is known in the art.
  • the preferred method of applying the coating composition of the present inve ntion to a supporting substrate, particularly a valve metal substrate involves the thermochemical deposition of the coating in a number of successive layers.
  • salts of the various component metals are dissolved, for example in alcohol, and applied, as by painting onto the substrate.
  • the solution-coated substrate is then heated to an elevated temperature in the presence of oxygen to thermochemically convert the salts into the desired chemical and physical form.
  • Successive layers e.g., 4-l 2, are applied in this manner until the desired coating thickness is obtained.
  • the coated substrate is preferably subjected to a post-bake treatment at an elevated temperature which treatment further orders the crystals. It has been noted that electrodes subjected to this post-bake exhibit improved wear-rates. It is thought to be surprising that crystalline cobalt metatitanate results from this procedure since known means for production of same generally require temperatures within the range of 800-l000C.
  • a preferred method of preparing an electrode comprises:
  • thermochemical conversion of the last solution application heating the substrate to a temperature of 525575C for from 5 to 10 minutes.
  • wear-rates are determined by applying the coatings to a six inch square expanded titanium substrate and employing same as the anode in a horizontal mercury cell.
  • the anode-cathode gap is established at 0.15 inch, the current density at 6 amperes per square inch, the temperature of the brine (290 grams per liter aqueous sodium chloride) at 160F., the brine flow rate at 425 milliliters per minute and the mercury flow rate at 450 milliliters per minute.
  • the anode Prior to insertion in the cell, the anode is repeatedly washed, dried and weighed until weights agreeing within 0.1 milligram are obtained. Operation is then commenced and the anodes are removed when desired, usually every operating hours, and reweighed to the same criteria, the difference representing the wear of the anode.
  • Coating solutions are prepared by dissolving tetrabutyl orthotitanate, RuCl .2.5 H 0 and CoCl .6I-I O in normal butyl alcohol containing about 6 percent by volume of 36 percent I-ICl.
  • the amounts of the titanium, ruthenium and cobalt salts used are those sufficient to give the mole ratios indicated in Table 1, i.e., for Sample E, 317, 63 and 47 grams per liter, respectively, of the titanium, cobalt and ruthenium salts are used.
  • Six coats of each solution are applied to clean titanium mesh substrates with heating after each application in air to a temperature of 450C.
  • thermochemical decomposition is effected at 300C and the post-bake temperature is 600C.
  • the values given for chlorine potential are obtron.
  • X-ray analysis shows the following coating characteristics El) rutile solid solution (TiO --RuO no crystalline cobalt compounds; E2) rutile solid solution, crystalline cobalt metatitanate, E3) rutile solid solution, crystalline cobalt metatitanate.
  • the chlorine potential of sample E3, measured at 6 a.s.i., is 0.06 volt higher than sample E2.
  • a solubility test conducted by boiling the samples for 10 minutes in 10 volume percent HCl indicates that 0.40 milligram of ruthenium and 4.5 milligrams of cobalt are leached from sample El whereas only 0.13 and 3.2 milligrams, respectively, are leached from E2 and E3.
  • a method of preparing an electrode which comprises:
  • thermochemical conversion of the last solution application heating the substrate to a temperature of 525-575C for from 5 to 10 minutes,
  • an electrode bearing on at least a portion of its surface an electrically-conductive, electro-catalytically-active coating consisting essentially of a coherent mixture of crystalline cobalt metatitanate and a titanium dioxide-ruthenium dioxide solid solution.
  • titanium, ruthenium and cobalt salts are, respectively, butyl titanate, ruthenium chloride and cobalt chloride.
  • Step (b) is about 450C.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
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  • Organic Chemistry (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Abstract

A coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution is provided. Typical use of the mixture is as an adherent, electrically-conductive, electrocatalytically-active coating applied to an electrically-conductive substrate for use as an electrode.

Description

United States Patent 1191 Kolb et a1.
[ 1 Dec.2,1975
1 1 METHOD OF MAKING AN ELECTRODE HAVING A COATING OF COBALT METATITANATE THEREON [75] Inventors: James M. Kolb, Mentor; Kevin J.
OLeary, Cleveland Heights, both of Ohio [73] Assignee: Electronor Corporation, Panama City, Panama [22] Filed: July 31, 1973 [21] Appl; No.: 384,210
Related U.S. Application Data [60] Division of Ser. No. 222,995, Feb. 2, 1972, Pat. No. 3,778,363, which is a continuation-in-part of Scr. No. 104,743, Jan. 7, 1971, abandoned.
[52] U.S. Cl. 427/126; 204/290 F; 427/226; 427/374; 427/372 [51] Int. Cl. B44D 1/18 [58] Field of Search 117/201, 215, 221; 204/290 F; 427/126, 226, 372, 374
[56] References Cited UNITED STATES PATENTS 3,399,966 9/1968 Suzuki et a1. 117/221 FOREIGN PATENTS OR APPLICATIONS 1,147,442 4/1969 United Kingdom 204/290 F Primary Examiner-Cameron K. Weiffenbach Attorney, Agent, or Firm-Hammond & Littell [57] ABSTRACT A coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution is provided. Typical use of the mixture is as an adherent, electrically-conductive, electrocatalyti- Cally-active coating applied to an electricallyconductive substrate for use as an electrode.
8 Claims, N0 Drawings METHOD OF MAKING AN ELECTRODE HAVING A COATING OF COBALT METATITANATE THEREON REFERENCE TO A COPENDING APPLICATION This is a divisional application of our copending application Ser. No. 222,995 filed Feb. 2, 1972, now US. Pat. No. 3,778,363 which in turn is a continuation-inpart of our copending Ser. No. 104,743, filed Jan. 7. 1971, now abandoned.
BACKGROUND OF THE INVENTION In the search for a satisfactory dimensionally stable electrode for use in a number of commercial electrolytic processes an electrode has recently been developed which has met with considerable commercial success. This electrode consists in general of a valve metal substrate bearing on its surface a valve metal oxideplatinum metal oxide solid solution-type coating. In such coatings, atoms of platinum metal are randomly substituted for atoms of valve metal in the characteristic rutile valve metal oxide crystal lattice. Such electrodes exhibit remarkably low potentials when employed in a variety of electrolytic processes, e.g., as anodes for the production of chlorine by electrolysis of sodium chloride solutions. A further advantage of such electrodes is that they exhibit a relatively low wearrate, that is, only a small amount of plantinum metal is consumed per ton of product manufactured.
Such electrodes are not entirely without disadvantage, however, in that owing to the amount of platinum metal required to be incorporated in the coating, the electrodes are expensive to fabricate. In addition, while the wear-rate is low, generally, for example, on the order of 0.10-0.15 gram of platinum metal per ton of chlorine produced, considering the tonnages involved a significant amount of platinum metal is irretrievably lost. Further, once the platinum metal content of these solid solutions coatings is substantially depleted, the electrodes become inactive. Hence, the cell must be disassembled for removal and replacement of the electrodes. For these reasons, the search for a coating material exhibiting all the advantages of the solid solutiontype coating, with the further advantage of a reduced wear-rate, continues.
STATEMENT OF THE INVENTION Therefore it is an object of the present invention to reduce the amount of platinum metal required in a valve metal oxide-platinum metal oxide solid solution without an attendant increase in potential.
It is a further object of the present invention to provide a material suitable for use as an electrode coating and having a reduced platinum metal wear-rate.
These and further objects of the present invention will become apparent to those skilled in the art from the specification and claims which follow.
A composition has now been found which is especially useful for application as an electrode coating, which composition consists essentially of a coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution. When applied to a supporting substrate, especially an electrically-conductive supporting substrate and particularly a valve metal substrate, an electrode is obtained which exhibits a low potential and which has extremely low platinum metal wear-rates.
2 It has further been found that such an electrode is particularly effective if applied in a manner which allows rapid initial heating of the coating during formation and subsequent post-treatment at an elevated tem- 5 perature. In this manner, the physical form of the cobalt metatitanate is apparently optimized, resulting in a particularly durable coating.
The invention finds particular advantage when the coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-platinum metal oxide solid solution is applied to a valve metal base, the resulting structure being used as an anode for the production of chlorine by electrolysis of brine. In this manner, a reduction in the amount of platinum metal required per square foot of anode surface is possible, without sacrifree in the potential at which chlorine is discharged at the anode face. Surprisingly, the anode has a significantly lower platinum metal wear-rate per ton of chlorine produced.
DESCRIPTION OF THE PREFERRED EMBODIMENTS A sample electrode has been prepared as is described more fully hereinbelow by application to a clean titanium substrate of a solution containing salts of titanium, ruthenium and cobalt. The electrode exhibits re markable adhesion between the coating and the substrate. Examination by X-ray diffraction indicates, in addition to the presence of the characteristic rutile Ti- O solid solution crystal structure, that there is also present crystalline cobalt metatitanate as a separate phase dispersed throughout the solid solution. It is apparent from the results obtained that the cobalt metatitanate in some manner stabilizes the solid solution, thus preventing normal wear to a great extent. To qualify as crystalline for the purpose of this invention the metatitanate, when subjected to X-ray diffraction analysis, must exhibit peaks characteristic of cobalt metatitanate. It is not necessary that the crystals be highly ordered, although this is preferred, only sufficiently so that discemable peaks are evidenced. While cobalt metatitanate having at least some degree of crystallinity is required and constitutes the invention in admixture with the solid solution, cobalt oxides and/or amorphous cobalt titanate may be present without substantial detriment. As is explained more fully hereinbelow, the extent of cobalt titanate crystallinity appears to depend upon the various heat treatments to which the electrode is subjected during preparation.
The solid solutions contemplated by the present invention have been described as valve metal oxideplatinum metal oxide solid solutions. By valve metal it is intended to refer to titanium, tantalum, zirconium and niobium, while by platinum metal the reference is to platinum, palladium, ruthenium, iridium, rhodium and osmium.
The quantities of the various ingredients of the composition of the present invention are conveniently expressed in terms of the mole ratios of the various metals present. Thus the ratio of valve metal to platinum metal plus cobalt should be within the range of 5: 1-1 :5 while the ratio of platinum metal to cobalt should be within the range of 4:1- 2:3. A preferred range, especially when dealing with titanium, ruthenium and cobalt is, respectively, 10:2:3. Expressed another way, the crystalline cobalt metatitanate will constitute up to 35%, preferably 10-35%, still more preferably 25-35%, by weight, of the total solid solution plus crystalline cobalt 3 metatitanate.
Generally the use of the compositions of the present invention will be as a coating applied to a conductive substrate. However, the material itself, absent a substrate, will find some application. Techniques for preparation are in many respects standard to the preparation of solid solutions, with the additional inclusion of a cobalt compound. For example sealed tube or flame spray techniques may be applied. The material thus obtained has a high degree of non-selective catalytic activity thus suggesting its use for the catalytic destruction of organic compounds, such as in exhaust emission. Alternately, the material may be impregnated into porous graphite for use as a fuel cell electrode or dispersed in an organic binder, such as a fluorocarbon binder, to prepare a porous electrode, again useful in fuel cells. Other applications will suggest themselves to those skilled in the art.
Generally, however, the composition finds applica tion as a coating on a supporting substrate. Since the coating will not generally be sufficiently massive to conduct current from the primary souce, an electrically-conductive substrate will be employed. Additionally, the substrate will be one which, upon the possible mechanical failure of the applied coating, will be inert to the environment in which it is employed. Preferably, at least when use is to be as an anode for the production of chlorine, the substrate will be a valve metal, typically titanium. The physical configuration of the supporting substrate is independent of the present invention and depends primarily upon the cell design in which the electrode is to be employed. It is also quite possible to apply the coating to a substrate to which there has previously been applied a protective or barrier layer to achieve a desired chemical or physical effect, for example, a manganese dioxide layer serving to prevent the diffusion of oxygen through the coating to the underlying substrate. Alternately, protective ceramic layers may be applied over the coating, as is known in the art.
While the invention is not so limited, the preferred method of applying the coating composition of the present inve ntion to a supporting substrate, particularly a valve metal substrate, involves the thermochemical deposition of the coating in a number of successive layers. Generally in such a technique, salts of the various component metals are dissolved, for example in alcohol, and applied, as by painting onto the substrate. The solution-coated substrate is then heated to an elevated temperature in the presence of oxygen to thermochemically convert the salts into the desired chemical and physical form. Successive layers, e.g., 4-l 2, are applied in this manner until the desired coating thickness is obtained.
While the foregoing general technique has been used with success in the preparation of the usual unmodified solid solution-type coatings, it has been found that certain alterations in the procedure are required if crystalline cobalt metatitanate is to be obtained. Ordinarily the substrate with the applied solution is introduced relatively gradually into an oven and brought to the temperature required for thermochemical conversion. It has been found that to prepare a crystalline cobalt metatitanate-modified coating, however, it is necessary to raise the temperature of the substrate rapidly to within the desired final range. In this manner, a larger proportion of cobalt metatitanate in the desired crystalline structure, as opposed to oxides or amorphous titanates, is formed. In addition, it has been found that, after application of the last solution coating and conversion to the desired chemical form, the coated substrate is preferably subjected to a post-bake treatment at an elevated temperature which treatment further orders the crystals. It has been noted that electrodes subjected to this post-bake exhibit improved wear-rates. It is thought to be surprising that crystalline cobalt metatitanate results from this procedure since known means for production of same generally require temperatures within the range of 800-l000C.
Thus, for example, a preferred method of preparing an electrode comprises:
a. applying a solution of salts of titanium, ruthenium and cobalt to an electrically-conductive substrate;
b. rapidly inserting the substrate with applied solution into an oven at a temperature within the range of 425475C and in the presence of oxygen;
c. maintaining the substrate at the oven temperature for a period of time sufficient to thermochemically convert the salts to the desired chemical state;
d. cooling the substrate;
e. applying any desired number of coatings of said solution in the same manner and,
f. after thermochemical conversion of the last solution application, heating the substrate to a temperature of 525575C for from 5 to 10 minutes.
In order that those skilled in the art may more readily understand the present invention, the following specific examples are afforded. In these examples, wear-rates are determined by applying the coatings to a six inch square expanded titanium substrate and employing same as the anode in a horizontal mercury cell. The anode-cathode gap is established at 0.15 inch, the current density at 6 amperes per square inch, the temperature of the brine (290 grams per liter aqueous sodium chloride) at 160F., the brine flow rate at 425 milliliters per minute and the mercury flow rate at 450 milliliters per minute. Prior to insertion in the cell, the anode is repeatedly washed, dried and weighed until weights agreeing within 0.1 milligram are obtained. Operation is then commenced and the anodes are removed when desired, usually every operating hours, and reweighed to the same criteria, the difference representing the wear of the anode.
EXAMPLE 1 Coating solutions are prepared by dissolving tetrabutyl orthotitanate, RuCl .2.5 H 0 and CoCl .6I-I O in normal butyl alcohol containing about 6 percent by volume of 36 percent I-ICl. The amounts of the titanium, ruthenium and cobalt salts used are those sufficient to give the mole ratios indicated in Table 1, i.e., for Sample E, 317, 63 and 47 grams per liter, respectively, of the titanium, cobalt and ruthenium salts are used. Six coats of each solution are applied to clean titanium mesh substrates with heating after each application in air to a temperature of 450C. The temperature of the substrate is brought rapidly (one minute or less) to temperature, which is maintained for seven minutes. After application of the last coating, samples B-F are post-baked for 7 minutes at 550C. Sample A is not so treated since it is known that heating at elevated temperatures has an adverse effect upon the potential of standard solid solution-type coatings. On the other hand, in Sample G thermochemical decomposition is effected at 300C and the post-bake temperature is 600C. The values given for chlorine potential are obtron.
TABLE I Moles Moles Moles Sample Ti Ru Co C0 C1 Substitution Potential F 2 0.2 0.8 80 l .49 G 2 0 l 100 l 5 EXAMPLE 2 This example illustrates the importance of temperature control in the thermochemical deposition method of the present invention. Anodes are prepared as in Sample E of Example 1 with the exception that (a) Sample El is merely baked between coats for seven minutes at 450C; (b) Sample E2 is baked for seven minutes between coats at 450C and post-baked for seven minutes at 550C and, (c) Sample E3 is baked for seven minutes between coats is 550C. X-ray analysis shows the following coating characteristics El) rutile solid solution (TiO --RuO no crystalline cobalt compounds; E2) rutile solid solution, crystalline cobalt metatitanate, E3) rutile solid solution, crystalline cobalt metatitanate. The chlorine potential of sample E3, measured at 6 a.s.i., is 0.06 volt higher than sample E2. Furthermore, a solubility test conducted by boiling the samples for 10 minutes in 10 volume percent HCl indicates that 0.40 milligram of ruthenium and 4.5 milligrams of cobalt are leached from sample El whereas only 0.13 and 3.2 milligrams, respectively, are leached from E2 and E3.
EXAMPLE 3 In this example, certain of the samples from Examples l and 2 are subjected to the wear-rate test previously described with the results shown in Table 11.
TABLE 11 TABLE ll-c0ntinued Cumulative Wt. Loss (mg) at V (hrs.) 6 a.s.i. After 500 Sample Co 200 300 Hrs.
D 50 1.8 4.3 5.4 1.42 E2 60 1.9 3.0 4.5 1.48 E1* 60 8.8 13.4 17 1.50
*No post-bake Two conclusions are reached. The crystalline cobalt metatitanate-modified solid solution coatings are superior to the unmodified coatings of the prior art insofar as wear-rate is concerned, often without a sacrifice in voltage. Further, while its voltage is still favorable, a cobalt-modified coating, absent the post-bake treatment and hence non-crystalline, exhibits a high wearrate (E1).
Although the invention has been described with reference to certain preferred embodiments thereof, it is not to be so limited since changes and alterations may be made therein which are still within the full and intended scope of the appended claims.
We claim:
1. A method of preparing an electrode which comprises:
a. applying a solution of salts of titanium, ruthenium and cobalt to an electrically-conductive substrate;
b. rapidly heating the substrate with applied solution to a temperature within the range of 425475C and in the presence of oxygen;
c. maintaining the substrate at the said temperature for a period of time sufficient to thermochemically convert the salts to a coherent mixture of crystalline cobalt metatitanate with a valve metal oxide-precious metal oxide solid solution;
d. cooling the substrate;
e. applying any desired number of coatings of said solution in the manner of steps (a) to (d) and,
f. after thermochemical conversion of the last solution application, heating the substrate to a temperature of 525-575C for from 5 to 10 minutes,
whereby there is obtained an electrode bearing on at least a portion of its surface an electrically-conductive, electro-catalytically-active coating consisting essentially of a coherent mixture of crystalline cobalt metatitanate and a titanium dioxide-ruthenium dioxide solid solution.
2. A method as in claim 1 wherein the titanium, ruthenium and cobalt salts are, respectively, butyl titanate, ruthenium chloride and cobalt chloride.
3. A method as in claim 1 wherein the titanium, ruthenium and cobalt salts are used in amounts sufficient to provide a mole ratio in solution of titanium; ruthenium plus cobalt within the range of 5: 1-l :5 and a ratio of ruthenium; cobalt within the range of 421-223.
4. A method as in claim 1 wherein the temperature in Step (b) is about 450C.
5. A method as in claim 1 wherein the temperature in Step (f) is about 550C.
6. A method as in claim 1 wherein according to Step (e) from 4-12 coats are applied.
7. A method as in claim 1 wherein the substrate is a valve metal substrate.
8. A method as in claim 1 wherein the substrate is ti-

Claims (8)

1. A METHOD OF PREPARING AN ELECTRODE WHICH COMPRISES: A. APPLYING A SOLUTION OF SALTS OF TITANIUM, RUTHENIUM AND COBALT TO AN ELECTRICALLY-CONDUCTIVE SUBSTRATE; B. RAPIDLY HEATING THE SUBSTRATE WITH APPLIED SOLUTION TO A TEMPERATURE WITHIN THE RANGE OF 425*-475*C AND IN THE PRESENCE OF OXYGEN C. MAINTAINING THE SUBSTRATE AT THE SAID TEMPERATURE FOR A PERIOD OF TIME SUFFICIENT TO THERMOCHEMICALLY CONVERT THE SALTS TO A COHERENT MIXTURE OF CRYSTALLINE COBALT METATITANATE WITH A VALVE METAL OXIDE-PRECIOUS METAL OXIDE SOLID SOLUTION D. COOLING THE SUBSTRATE; E. APPLYING ANY DESIRED NUMBER OF COATINGS OF SAID SOLUTION IN THE MANNER OF STEPS (A) TO (D) AND, F. AFTER THERMOCHEMICAL CONVERSION OF THE LAST SOLUTION APPLICATION, HEATING THE SUBSTRATE TO A TEMPERATURE OF 525*-575*C FOR FROM 5 TO 10 MINUTES, WHEREBY THERE IS OBTAINED AN ELECTRODE BEARING ON AT LEAST A PORTION OF ITS SURFACE AN ELECTRICALLY-CONDUCTIVE, ELECTROCATALYTICALLY-ACTIVE COATING CONSISTING ESSENTIALLY OF A COHERENT MIXTURE OF CRYSTALLINE COBALT METATITANATE AND A TITANIUM DIOXIDE-RUTHENIUM DIOXIDE SOLID SOLUTION.
2. A method as in claim 1 wherein the titanium, ruthenium and cobalt salts are, respectively, butyl titanate, ruthenium chloride and cobalt chloride.
3. A method as in claim 1 wherein the titanium, ruthenium and cobalt salts are used in amounts sufficient to provide a mole ratio in solution of titanium; ruthenium plus cobalt within the range of 5:1-1:5 and a ratio of ruthenium; cobalt within the range of 4:1-2:3.
4. A method as in claim 1 wherein the temperature in Step (b) is about 450*C.
5. A method as in claim 1 wherein the temperature in Step (f) is about 550*C.
6. A method as in claim 1 wherein according to Step (e) from 4-12 coats are applied.
7. A method as in claim 1 wherein the substrate is a valve metal substrate.
8. A method as in claim 1 wherein the substrate is titanium.
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Cited By (4)

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Publication number Priority date Publication date Assignee Title
US4056654A (en) * 1975-07-24 1977-11-01 Kkf Corporation Coating compositions, processes for depositing the same, and articles resulting therefrom
US4220884A (en) * 1978-05-01 1980-09-02 Trw Inc. Carbon brush for motors and method of making the same
US4431686A (en) * 1980-02-05 1984-02-14 Sigri Elektrographit Gmbh Method for coating a porous electrode
US6001225A (en) * 1996-10-31 1999-12-14 Bushman; James B. Catalytically coated anodes

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US3399966A (en) * 1964-05-18 1968-09-03 Trurumi Soda Company Ltd Novel cobalt oxide and an electrode having the cobalt oxide coating
US3505118A (en) * 1966-12-05 1970-04-07 Du Pont Fuel cell and process for producing electric current using titanium dioxide catalyst
US3632498A (en) * 1967-02-10 1972-01-04 Chemnor Ag Electrode and coating therefor
US3645862A (en) * 1967-09-26 1972-02-29 Imp Metal Ind Kynoch Ltd Method of making an electrode
US3684543A (en) * 1970-11-19 1972-08-15 Patricia J Barbato Recoating of electrodes
US3711397A (en) * 1970-11-02 1973-01-16 Ppg Industries Inc Electrode and process for making same
US3711382A (en) * 1970-06-04 1973-01-16 Ppg Industries Inc Bimetal spinel surfaced electrodes
US3809630A (en) * 1970-06-20 1974-05-07 Oronzio De Nora Impianti Electrolysis cell with permeable valve metal anode and diaphragms on both the anode and cathode
US3810770A (en) * 1967-12-14 1974-05-14 G Bianchi Titanium or tantalum base electrodes with applied titanium or tantalum oxide face activated with noble metals or noble metal oxides

Patent Citations (9)

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Publication number Priority date Publication date Assignee Title
US3399966A (en) * 1964-05-18 1968-09-03 Trurumi Soda Company Ltd Novel cobalt oxide and an electrode having the cobalt oxide coating
US3505118A (en) * 1966-12-05 1970-04-07 Du Pont Fuel cell and process for producing electric current using titanium dioxide catalyst
US3632498A (en) * 1967-02-10 1972-01-04 Chemnor Ag Electrode and coating therefor
US3645862A (en) * 1967-09-26 1972-02-29 Imp Metal Ind Kynoch Ltd Method of making an electrode
US3810770A (en) * 1967-12-14 1974-05-14 G Bianchi Titanium or tantalum base electrodes with applied titanium or tantalum oxide face activated with noble metals or noble metal oxides
US3711382A (en) * 1970-06-04 1973-01-16 Ppg Industries Inc Bimetal spinel surfaced electrodes
US3809630A (en) * 1970-06-20 1974-05-07 Oronzio De Nora Impianti Electrolysis cell with permeable valve metal anode and diaphragms on both the anode and cathode
US3711397A (en) * 1970-11-02 1973-01-16 Ppg Industries Inc Electrode and process for making same
US3684543A (en) * 1970-11-19 1972-08-15 Patricia J Barbato Recoating of electrodes

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4056654A (en) * 1975-07-24 1977-11-01 Kkf Corporation Coating compositions, processes for depositing the same, and articles resulting therefrom
US4220884A (en) * 1978-05-01 1980-09-02 Trw Inc. Carbon brush for motors and method of making the same
US4431686A (en) * 1980-02-05 1984-02-14 Sigri Elektrographit Gmbh Method for coating a porous electrode
US6001225A (en) * 1996-10-31 1999-12-14 Bushman; James B. Catalytically coated anodes

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