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Primary Examiner: Welsh, John D.
Assistant Examiner:
Attorney:
Claims: What is claimed is:

1. A coated article formed by electroless plating comprising a co-deposited uniform dispersion of diamond particles secured by substantial nucleation within a metallic matrix comprising one of the group consisting of: (1) an alloy including a metal of the sub-group made up of nickel, cobalt and mixtures thereof with one of the elements phosphorus, boron and mixtures thereof and (2) elemental copper, deposited on a supporting substrate consisting of polymer, metal, ceramic or glass.

2. A method of forming a composite structure on an article by electroless plating comprising immersing said article in a stable electroless plating bath having a composition effecting concurrent deposition of particulate diamond dispersed in a metallic matrix comprising one of the group consisting of: (1) an alloy including a metal of the sub-group made up of nickel, cobalt and mixtures thereof with one of the elements phosphorus, boron and mixtures thereof and (2) elemental copper, while maintaining agitation of said bath retaining said particulate diamond in suspension, and removing said article carrying said composite structure from said bath when said composite structure has been plated out on said article in preselected amount.

3. A coated article formed by electroless plating consisting of a shaped substrate, a metallic matrix coating deposited on said shaped substrate, and a uniform dispersion of co-deposited diamond particles secured by nucleation bonding within said metallic matrix, wherein

1. said substrate is one of the group consisting of (a) an organic polymer, including reinforced organic polymers, (b) metals, (c) ceramics, (d) glass,

2. said metallic matrix consists primarily of at least one of the group consisting of (a) nickel, (b) cobalt, (c) copper, together with smaller proportions of other components commonly codeposited from electroless plating baths, and

3. said diamond particles constitute from 1 to 50% by volume of said metallic matrix, with a particle size ranging from about 0.1.mu. to about 75.mu., but predominantly in the size range between 0.5.mu. to 25.mu..

4. A coated article formed by electroless plating consisting of a shaped substrate, a metallic matrix coating deposited on said shaped substrate, and a uniform dispersion of co-deposited diamond particles secured by nucleation bonding within said metallic matrix, wherein

1. said substrate is one of the group consisting of (a) an organic polymer, including reinforced organic polymers, (b) metals, (c) ceramics, (d) glass,

2. said metallic matrix consists primarily of at least one of the group consisting of (a) nickel, (b) cobalt, (c) copper, together with smaller proportions of other components commonly codeposited from electroless plating baths, and

3. said diamond particles constitute from 1 to 50% by volume of said metallic matrix, with a particle size ranging from about 0.1.mu. to 75.mu. but predominantly in the size range between 0.5.mu. to 25.mu., and said diamond particles individually consist of many individual crystallities tightly bonded to one another in essentially unoriented pattern giving polycrystalline particles having many irregular projections, ledges and craters.

5. A coated article formed by electroless plating according to claim 3 wherein said article is a fluid jet provided with a discharge orifice.

6. A coated article formed by electroless plating according to claim 4 wherein said article is a fluid jet provided with a discharge orifice.
Descriptions:
Description: BRIEF SUMMARY OF THE INVENTION

Generally, this invention consists of a method for depositing on an article a coating containing at least one member of the group metals and metal alloys and incorporating therein particulate dispersed diamond comprising contacting the surface of the article with a stable electroless plating bath consisting essentially of: (1) an aqueous solution of soluble constituents of the group, (2) electroless reducing agent therefor, (3) a suspension of diamond particles in concentration in the range maintaining fluidity of the bath, (4) a stabilizer for the bath of concentration in the range from that sufficient to prevent decomposition of the bath upon addition of diamond particles thereto to that retaining plating capability of the bath, and (5) additives facilitating electroless plating per se, and maintaining the diamond particles in suspension throughout the bath during coating of the article for a time sufficient to produce a preselected depth of coating on the article, together with the product of the method.

DRAWINGS

The following drawings, some of which are reproductions of marked-up photomicrographs and some of which are partially schematic line drawings, depict the composite structures obtained, the wear tracks developed during running yarn frictional testing of the several types of structures, and the test apparatus and its component orientation with respect to test specimens, plus a preferred deposition apparatus, in which:

FIG. I is a typical photographic plan view (6340X) of an electroless Ni-B alloy/12.mu. synthetic diamond "A" composite with the several most important structural features indicated by characteristic numerals,

FIG. II is a typical photographic plan view (6480X) of an electroless Ni-B alloy/9.mu. natural diamond composite, with individual structural features identified,

FIGS. III(A)-(E), inclusive, are partially schematic representations of the Accelerated Wear Test apparatus employed, and the results obtained, in the evaluation of the best composite coatings laid down by this invention, as to which (A) is a plan view of the test apparatus, (B) is an inset perspective of the running yarn course over the surface of a specimen in test, (C) is a side elevation view, partly in section, taken on line IIIC-IIIC, FIG. IIIA, (D) is a perspective view of the relationship of running yarn line to specimen in an invalid Standard Test which yields corner notching [FIG. III(M)] without a wear track on the mid-specimen surface between the notches and III(E) [N] is a showing of a typical normal groove obtained during a valid Accelerated Wear Test,

FIG. IV is a typical photographic plan view (2860 X) of an electroless Ni-B alloy/9.mu. natural diamond composite indicating the diagonal running test yarn course and showing structural features as affected by the Standard Wear Test,

FIG. V is a typical photographic plan view (2640X) of an electroless Ni-B alloy/9.mu. synthetic diamond "A" composite indicating the running test yarn course and showing structural features as affected by the Accelerated Wear Test,

FIG. VI is a typical photographic plan view (250X) of an electroless Ni-B alloy/9.mu. synthetic diamond "A" specimen in the as-plated condition (A) and after an Accelerated Wear Test (B),

FIG. VII is a typical photographic plan view (250X) of an electroless Ni-B alloy/9.mu. natural diamond specimen in the as-plated condition (A) and after an Accelerated Wear Test (B),

FIG. VIII is a typical photographic plan view (250X) of an electroless Ni-B alloy/9.mu. synthetic diamond "B" specimen in the as-plated condition (A) and after an Accelerated Wear Test (B),

FIG. IX is a sectional perspective view of a preferred embodiment of apparatus which is employed to lay down the composite coatings of this invention,

FIG. X is a fragmentary, cross-sectional, side elevation view of a multi-filament yarn interlacing air jet which is advantageously coated according to this invention,

FIG. XI is an end elevation view, partly in cross section, of a multiplicity of interlacing jets of the design of FIG. X in assembled relationship, and

FIG. XII is a section on line XII--XII, FIG. XI.

INTRODUCTION

The prior art is replete with publications teaching the electroplating of metallic-diamond composite coatings; however, it is believed that electroless plating of diamond composites has never been successfully accomplished except, possibly, by the very special technique taught in application Ser. No. 103,355, assigned to common assignee, of which one of the present applicants is a co-inventor. There is, it is true, art on the electroless plating of composites of metals and particulate metal compounds, specifically, British Pat. No. 1,219,813 (corresponding to U.S. Pat. No. 3,617,363); however, there appears to be nothing with respect to particulate diamond.

Applicants' composite laydowns must be distinguished from electroless coating of diamond particles per se with nickel and cobalt, such as taught in U.S. Pat. No. 3,556,839.

Applicants have now discovered a method of concurrently depositing, by the electroless plating technique, as a disperse phase, particulate diamond in composite with Ni(B), Ni(P), Co(B), Co(P) and other metals and metal alloys singly, or as mixtures of any two or more of these substances together, as well as metallic copper as the continuous phase or matrix. The coatings produced are highly adherent, relatively non-porous and possessed of a truly remarkable abrasive wear resistance. In addition, the diamond particle pull-out characteristics, particularly of the synthetic diamond species "A" hereinafter described, are very good, so that objectionable detritus is not carried over into the surrounding environment which could, possibly, act as an abrasive agent to gall or otherwise damage the fine finish of bearings or other metal-to-metal contact surfaces. The combination of properties displayed by the diamond composites of this invention are such that they have great potential value as abrasion-resistant surfaces for both dry and wet service, writing instrument nibs, cutting tool surfaces, piston ring and other sliding contacting surfaces, textile wear surfaces and other extremely demanding uses.

Applicants have prepared composites incorporating, singly, particulate natural diamond and the only two synthetic diamonds which are commercially available at the time of filing, these being denoted synthetic diamond "A," which is explosively formed by applicants' assignee in accordance with the teachings of U.S. Pat. No. 3,401,019, and synthetic diamond "B," which is marketed by the General Electric Company, Schenectady, N. Y., and which is believed to be fabricated in accordance with the teachings of U.S. Pat. Nos. 2,947,608 through 2,947,611, inclusive.

As hereinafter described, the composites of applicant' invention are usually used as relatively thin self-adhered coatings deposited on the surfaces of a substrate consisting of a metal, polymer, ceramic, glass, wood or other relatively rigid material. However, if desired, the composites can be laid down on a temporary substrate, such as thin metal, water-resistant paper, film or foil, polymer sheeting or the like and the coating stripped therefrom (or the temporary substrate melted or dissolved away) and thereafter utilized as a wear-resistant shell per se, which can be adhered to any firm supporting base material which is, in itself, suited to the particular use environment's requirements, by adhesives, cement, heat treatment or in other conventional manner known to the art.

It is practicable to use a very wide variety of substrates and base materials, the only limitation being that inherent in widely different coefficients of thermal expansion as regards the coating with reference to the underlying support material. Filled polymers, such as those incorporating staple fibers as reinforcement, appear to give most satisfactory substrate structures.

Applicants have prepared composite coatings on substrates of unfilled ABS (acrylonitrile-butadiene-styrene copolymer), filled ABS, ABS reinforced with glass fibers and with acicular TiO.sub.2, polyimides, polyolefins, polyesters, "Delrin" acetal resins, "Zytel" nylon resins, and "Nomex" aromatic polyamide resins, and, while all have not been tested as thoroughly as some hereinafter described, all have supported coatings that were visually uniform and well-adhered.

Polymers are, of course, especially preferred in moderate temperature corrosive service environments, because of their low cost, relatively high resistance to corrosion and low contamination potentiality. On the other hand, where relatively high temperatures exist, or where it is necessary to improve the composite coating properties by heat treatment, metals are preferred, since they survive heating to relatively high temperatures without the warping and compositional deterioration usually suffered by polymers.

THE DEPOSITION PROCESS

The composite deposition process employed in this invention can utilize much of the published electroless plating art.

Thus, for electroless Ni-P min. strike deposition U.S. Pat. Nos. 2,658,841 and 2,658,842 are instructive. Similarly, electroless Ni-B, Ni-Co-B, and Co-B processes are taught in U.S. Pat. Nos. 3,062,666; 3,063,850; 3,096,182; 3,140,188; 3,234,031 and 3,338,726. Also, electroless Co-P and Ni-Co-P processes are disclosed in U.S. Pat. Nos. 2,532,284 and 2,871,142. Finally, electroless copper processes are described in U.S. Pat. Nos. 2,996,408; 3,075,855-6; 3,383,224; 3,431,120; 3,329,512; 3,361,580; 3,392,035; 3,457,089 and 3,453,123.

The electroless Ni-P processes which are the subjects of certain of the Patents cited supra utilize aqueous solutions containing H.sub.2 PO.sub.2 .sup.- ions, which act as the reducing agent, and nickel ions furnished by dissolved nickel salts. Similarly, the electroless Ni-B processes utilize aqueous solutions of nickel salts and a boron-containing reducing agent, such as BH.sub.4 .sup.- ions or dimethylamine borane (DMAB). In addition, workable electroless plating baths contain buffers, e.g., salts of weak carboxylic or dibasic acids, to prevent rapid changes in pH, plus at least one of a large variety of chemical compounds or metallic ions which act as stabilizers preventing spontaneous bath decomposition.

The foregoing mentioned components, and others, are commonly present in electroless plating baths, or are added during plating, for such purposes as: (1) adjustment of pH, (2) complexing of metal cations, (3) surface activity control, (4) bath efficiency control and (5) deposit internal stress control, and these are generally referred to herein as additives facilitating electroless plating per se.

Among the patent references cited supra are several teaching that other metallic or non-metallic elements, including (but not limited to) lead, zinc, thallium and arsenic may be co-deposited with the principal elements Ni, Co and Cu. It is also known that Ni, Cu and P can be collectively co-deposited using a proprietary process of the Shipley Company, Newton, Massachusetts.

More specifically, U.S. Pat. No. 3,140,188 teaches processes by which Ni and Co can be deposited from stable baths containing Zn or Fe, and that the coatings are smooth, adherent and constituted of alloys including: Ni-Zn, Ni-Co-Zn, Co-Fe, and Ni-Fe. Also, U.S. Pat. No. 3,062,666 teaches that a lead salt can be included in the plating bath as a stabilizer, and it has been verified that the Ni or Co plating from the bath of this Patent contains small quantities of Pb, without impairing the smoothness. Similarly, application Ser. No. 847,457, assigned to common assignee, teaches that thallium can be a component of smooth, adherent electroless plates if suitably incorporated in the bath. Moreover, U.S. Pat. No. 3,063,850 teaches that not only Ni and Co but also Cu, Cd and Sn individually can be plated as smooth adherent coatings by electroless plating.

Accordingly, the instant invention is not limited to electroless deposits consisting solely of the metals Ni, Co, Cu and the non-metals P and B, but also comprises these elements singly and plurally, as well as other elements whose presences are tolerable or, indeed, beneficial, as far as bath stability and coating quality are concerned.

Electroless plating is an autocatalytic process, in the sense that the coating which is deposited serves as catalyst for continuation of the plating process. Once plating is initiated on the surface of a metallic, ceramic, polymeric or other substrate, it will continue as long as the article remains in contact with the periodically replenished plating solution. Since no electric current is required for the plating which occurs, the general adjectives "electroless" or "chemical" have been used to differentiate these processes from conventional electroplating.

The diamond particles utilized in this invention can have particulate sizes in the range of from less than about 0.1 to 50.mu. or even to 75.mu.. The quantity of diamonds incorporated in our electroless alloy coatings can range from about 1 to about 50 volume per cent.

The diamond particle shapes employed herein were approximately equi-axed and there appeared to be no optimum particle size distribution. Thus, the diamonds employed in some of the Examples infra consisted of mixtures extending from about 1 to about 22.mu. size.

In the plating of electroless alloy-diamond composites according to this invention, a dispersion of diamond particles is maintained throughout the plating bath, so that the particles constantly contact surfaces of the substrates being coated. The plating baths must be properly formulated, controlled and operated as hereinafter described under conditions that prevent initiation of plating on the surfaces of the diamond particles suspended in the bath. Thus, if plating initiates on the surfaces of the suspended particles, the bath will decompose by rapid depletion of the metallic ions and the reducing agent, rendering the bath uncontrollable and useless for further plating. The plated diamond particles which come into contact with the substrates being coated form rough, highly porous, nonadherent, unsightly deposits, which are totally unacceptable. Thus, the object of our invention is completely different from that of U.S. Pat. No. 3,556,839 and also of common assignee's application Ser. No. 847,457, where the intent is to plate the surfaces of the diamond particles suspended in the plating bath.

Metallic substrates are given a conventional preplating treatment, depending on the particular metal or alloy, prior to coating by this invention. Thus, the steel specimens of the Examples infra were first solvent-degreased in trichlorethylene, followed by hot alkaline cleaning (e.g., Enbond S61) at 65.degree.C. for about 5 minutes, after which they were water rinsed, acid-etched in a 50% by volume solution of HCl at room temperature for 30 to 60 secs., and water rinsed prior to immersion in the plating bath.

Plating initiates spontaneously on metallic substrates which are catalysts for electroless plating processes. For example, for baths that deposit nickel alloys, catalytic metals include Co, Ni, Pt and Pd. Plating also initiates spontaneously on metals which are noncatalytic but less noble than the bath metal, because a thin film of the dissolved metal rapidly forms through displacement, and the dissolved metal, being a catalyst, continues the plating process. Examples of this, for electroless nickel processes, are the plating of iron, aluminum, magnesium, beryllium and titanium. Metallic substrates which do not initiate plating spontaneously can be initiated galvanically by brief application of a small negative potential to the substrate.

Nonconducting substrates, such as polymeric organic materials, are prepared for plating by roughening mechanically as by grit blasting (27 micron alumina being suitable), followed by a treatment depositing a suitable catalyst for electroless plating, typically immersion in an SnCl.sub.2 solution (70 g/l SnCl.sub.2 plus 40 cc/l HCl, 80.degree.F.), water rinsing and immersion in a PdCl.sub.2 solution (0.1 g/l PdCl.sub.2 plus 1cc/l HCl, 80.degree.F.) and water rinsing. Pearlstein, in Metal Finishing, August 1955, pp. 59-61, outlines a two-step approach to surface activation using the hereinbefore described SnCl.sub.2 predip and PdCl.sub.2 activation solution.

Numerous proprietary processes have been developed that combine and simplify the individual steps of the activation procedures. For example: (1) U.S. Pat. No. 3,563,784 teaches the preactivation step of immersing plastic parts in a surfactant solution to insure complete coverage with the electroless deposit of metal; (2) U.S. Pat. No. 3,579,365 teaches the pre-etch preactivation step of treating the polymer surfaces with colloidal or emulsified fatty-acid materials to improve metal adhesion; (3) U.S. Pat. No. 3,562,038 and British Pat. No. 1,212,002 teach two approaches to surface activation using colloidal suspensions of palladium particles prepared by pre-reduction of palladium chloride with stannous chloride. The foregoing processes extend the application of electroless plating techniques to a wide spectrum of polymers, including the polyolefins and polyesters.

Ni, Co PREPLATING TREATMENT

The ABS (i.e., acrylonitrile-butadiene-styrene copolymers), glass fiber-reinforced ABS and acicular rutile fiber-reinforced ABS resins described in the examples infra, which were given a plate with diamond particles composited with electroless Ni and electroless Ni-Co alloy matrices, were first given the following preplating treatment.

1. Cleaning by immersion in a proprietary alkaline cleaner (e.g., Marbon C-15) for 5 minutes at 65.degree.C., to remove any grease or oil picked up in molding or handling operations.

2. Rinsing in hot and cold water in the sequence recited for 30 secs. each.

3. Chemically roughening to promote coating adhesion by immersion for 4-6 minutes at 65.degree.C. with mild agitation in a proprietary chromic-sulfuric acid etch (e.g., Marbon E-20).

4. Rinsing in, first, hot and then cold water for 30 secs. each, followed by an ultrasonic water rinse of 2 minutes and a final rinse with running deionized water.

5. Sensitizing by immersion in a proprietary (Enplate 432) bath containing tin ions with the parts agitated in the bath.

6. Rinsing twice in de-ionized water for 30 secs. each while agitating gently to remove excess tin ions from the articles.

7. Immersing in a proprietary activation bath (e.g., Enplate - 440 ) containing Pd ions. The tin ions were here oxidized under gentle agitation for 1.5 minutes, thereupon reducing the Pd ions to metallic state.

8. Finally, rinsing with two separate de-ionized water rinses of 30 secs. duration each while gently agitating.

COPPER PREPLATE

ABS reinforced and unreinforced specimens employed in the examples infra, wherein particulate diamond was composited with an electroless Cu matrix, were given the following preplating treatment:

Steps 1 through 4 supra, then

5. Immersing in MacDermid, Inc. Metex PTH Activator 9070 at room temperature for 8 mins.

6. Rinsing twice in de-ionized water for 30 secs. duration each.

7. Immersing in Metex PTH Accelerator 9071 for 8 mins. at room temperature.

8. Finally, giving the articles two de-ionized water rinses of 30 secs. duration each.

Ceramic substrates are prepared for plating by first mechanical roughening, e.g., grit blasting, or by chemical roughening using an aqueous HF solution to develop anchoring points for the catalyst and for the wear-resistant electroless alloy strike that is subsequently applied.

STRIKE TREATMENT

All of the specimens of the examples (except as described for Ex. 20) were given a 10 to 70 minute plating strike prior to plating in the electroless alloy plating bath containing the diamond dispersion. The strike bath was of the same composition as the composite plating bath, except that it contained no diamond powder. The purpose of the plating strike is to insure that the adhesion of the initial electroless coating applied to the substrate is not adversely affected by abrasive or other action of the dispersed particles contained in the composite plating bath. A plating strike is imperative in plating non-conductors such as polymers, ceramics, wood and glass, the surfaces of which are thereby covered with adsorbed layers or islands of a catalyst initiating electroless plating. However, in the case of metallic substances displaying high activity in the plating bath, e.g., plain C steel, Ni, Co and Pd, the strike can be omitted.

The electroless alloy-diamond composite coatings of this invention can be deposited by a wide variety of plating techniques ranging from simple rack plating, wherein articles are supported by a rack, to barrel plating, wherein the articles are introduced as free bodies into a rotating bath container, which can have its axis horizontally disposed or somewhat inclined. In addition, of course, articles can be tumble-plated as taught in application Ser. No. 103,355 supra.

The diamond powder to be composited (0.5 to 100 gms. as desired) is first blended with about 200 to 400 ml. of the plating bath in a high-speed mixer to break up agglomerates, wet all of the particles and form a concentrated slurry containing a uniform dispersion of particles. The slurry is then slowly added to the plating vessel, where the powder particles are kept in suspension by mechanical agitation and/or bath circulation. The quantity of diamonds maintained in the suspension, while most commonly in the range of 1 to 10 g. per liter of bath, can range up to as much as 40 g./liter, the upper limit being only that the bath must remain sufficiently fluid to be capable of ready agitation and circulation.

In the experiments hereinafter reported as examples, the metallic ions, reducing agent and bath stabilizer were all replenished on a periodic basis as determined by wet or colorimetric chemical analyses for the respective reacting species.

RACK PLATER

One design of apparatus utilized in the preparation of specimens for Examples 6, 7, 8, 19-22, and 26-28, inclusive, was the rack plater shown somewhat schematically in FIG. IX of the drawings.

Referring to FIG. IX, the plating vessel 10 was a glass jar of 9 liters capacity, about 22 cm. inside diameter, which was provided with two annular shelves 11 and 12, fabricated from polytetrafluoroethylene, these shelves being held horizontal by snug frictional through-bore mounting on three upstanding polytetrafluoroethylene posts 16, only two of which appear in the FIGURE.

Shelves 11 and 12 typically measured 13 cm. inside diameter, 20 cm. outside diameter and were 0.6 cm. thick. Upper shelf 11 was apertured at four locations 17 spaced 90.degree. apart circumferentially, each sized to snugly engage a sample approximately 0.635 cm. .times. 1.52 cm., so that the top and bottom faces were exposed to the plating solution for the simultaneous plating of these two surfaces. Lower shelf 12 was provided on its upper face with a multiplicity of recesses 18, which did not extend all the way through the shelf, these recesses being dimensioned to closely fit the specimens 20, which were snugly set therein, so that only the upper exposed surfaces were plated.

An electric motor-driven stirrer (typically, 350 rpm) provided the bath agitation, the shaft 22 of which was disposed approximately concentric with the longitudinal axis of vessel 10, which stirrer was provided, at its horizontally bent lower end, with an upstanding elliptical paddle 23 having a major axis of 6.25 cm. and a minor axis of 2.5 cm. The dimensions a, b and c denoted in FIG. IX are, typically, 1.90, 2.54 and 7.62 cms., respectively.

EXAMPLES

General details as to the specimens prepared for typical individual examples are provided in the following Tables:

                                      Table 1A
    __________________________________________________________________________
    Description of Specimens in Examples on Plating Polymers
    Recessed Samples.sup.1
                     Coupons.sup.2
                             Blocks.sup.3
                                     Other
    Example      FR-     FR-     FR- FR-ABS
    Number
          ABS    ABS ABS ABS ABS ABS Parts Total
    __________________________________________________________________________
     1    1      2   3   3   3   3   0     15
    (TPC-40)
     2    1      2   5   5   3   3   0     19
    (TPC-32)
     3    1      2   3   3   3   3   0     15
    (TPC-39)
     4    1      2   3   3   3   3   0     15
    (TPC-36)
     5    1      2   3   3   3   3   0     15
    (TPC-46)
     9    1      2   5   5   3   3   0     19
    (TPC-33)
    10    1      2   5   5   3   3   0     19
    (TPC-34)
    11    1      2   5   5   3   5   0     21
    (TPC-28)
    12    0      0   0   0   0   0   2 jet caps
                                            2
    13    1      0   0   6   1   1   6 venturi
                                           15
    (TPC-35)                         units
    14    0      0   1   1   1   1   0       4
    (RPC-11)
    15    1      2   3   3   3   3   0     15
    (TPC-42)
    16    1      2   5   5   3   5   0     21
    (TPC-27)
    17    1      2   3   3   3   3   0     15
    (TPC-44)
    18    1      2   3   3   3   3   0     15
    (TPC-45)
    23    1      2   5   5   3   3   0     19
    (TPC-30)
    __________________________________________________________________________
               Abbreviations: applicable to Table 1A:
    TPC --      Tumble-plated composites
    RPC --      Rack-plated composites
    ABS:        acrylonitrile-butadiene-styrene
    FR-ABS:     fiber-reinforced acrylonitrile-butadiene-styrene
    __________________________________________________________________________
     Footnotes:
      .sup.1 The recessed-samples contained small diameter holes and slots.
      .sup.2 The dimensions of the coupons were 3 .times. 10 .times. 19 mm.
      .sup.3 The dimensions of the blocks were 8 .times. 13 .times. 25 mm.


Table 1B ______________________________________ Description of Specimens in Examples of Plating Steel Number of Specimens Plated Yarnline Number Blocks.sup.1 Block.sup.2 Washer.sup.3 Total ______________________________________ 6 (RPC-6) 11 1 3 15 7 (RPC-7) 11 1 3 15 8 (RPC-12) 11 1 3 15 19 (PRC-3) 2 2 0 4 20 (RPC-20) 2 1 0 3 21 (RPC-21) 2 1 0 3 22 2 2 0 4 ______________________________________ .sup.1 Dimensions of rectangular blocks (6 mm .times. 10 mm .times. 15 mm .sup.2 Dimensions of rectangular yarnline wear block (6 mm .times. 6 mm .times. 12 mm) .sup.3 Dimensions of cylindrical thrust washer: Diameter: 31 mm Height: 9 mm

Table 1C ______________________________________ Weights of Samples Plated Individual Weights, Designation & Material grams ______________________________________ "TP" samples 0.6 to 0.9 ABS coupons 0.60 FR-ABS coupons 0.65 ABS blocks 2.6 FR-ABS blocks 3.2 Steel blocks 8.1 Steel yarnline wear block 3.6 Thrust washers 58 ______________________________________

Table 1C ______________________________________ Weights of Samples Plated Individual Weights, Designation & Material grams ______________________________________ "TP" samples 0.6 to 0.9 ABS coupons 0.60 FR-ABS coupons 0.65 ABS blocks 2.6 FR-ABS blocks 3.2 Steel blocks 8.1 Steel yarnline wear block 3.6 Thrust washers 58 ______________________________________

Table 1D __________________________________________________________________________ Characteristics of Particulate Solids Incorporated Into Electroless Coatings in the Several Examples Nominal Maximum.sup.1 Nominal Size Size % % Example Diamond or Size, Range, Limit Over- Under- Numbers Other Powder .mu. .mu. .mu. size size __________________________________________________________________________ 1,9,14, "A" 9 6 - 12 14 .about.3** .about.13** 15,19,20 2,10 natural 9 6 - 12 14 <5** <20** 3 "B" 9 6 - 12 14 <5** <20** 4 .alpha.-Al.sub.2 O.sub.3 8 -- -- -- -- 5 .alpha.-SiC 6 1 - 10 None 20* 25* 6,8 "A" 1 0 - 2 3 .about.3** .about.13** 7 natural 1 0 - 2 3 <5** <20** 11,12,13 "A" 3 2 - 4 5 .about.3** .about.13** 16,17,18 "A" 5 2 - 8 None <10* <10* 21,25 "A" 6 4 - 8 10 .about.3** .about.13** 22 "A" 9 6 - 12 14 <5** <20** 23 "A" 17 12 - 22 None <15* <15* 24 .alpha.-Al.sub.2 O.sub.3 14 6 - 21 30 -- -- __________________________________________________________________________ .sup.1 No particle exceeded the maximum size limit when one is specified. **Percentage of number of particles above upper limit of nominal size range (oversize) or below lower limit of nominal size range (undersize). *Weight per cent of powder above upper limit (oversize) or below lower limit (undersize) of nominal size range.


The plating process utilized in Examples 1-5, inclusive, was identical, except that differrent types of powders were added to the bath as indicated in the foregoing Table 1D. In each Example a number (typically, 15-19) of molded ABS, glass-reinforced ABS, and acicular rutile-reinforced ABS polymer articles were tumble-plated as taught in appl'n Ser. No. 103,355 supra, which is incorporated herein by reference. (The acicular rutile is a powder produced by the Pigments Department, E. I. du Pont de nemours Co., which consists of single crystals of TiO.sub.2 measuring about 0.2.mu. wide .times. 2 to 3.mu. long.) The plating was conducted in an inverted frustoconical funnel of included angle 46.degree. measuring 24 cm in diameter across at the top end and 0.93 cm across the lower spout end, 25 cm high, plating solution being circulated continuously through the spout upwardly into the funnel portion with overflow out of the top collected in a surrounding sump. The plating solution velocity was maintained at a high enough rate (typically 4,200 cm 3/min.) to support the articles being plated and, at the same time, tumble them slowly in a random manner at a rate of 4 to 7 complete inversions per minute. However, the tumble rate is a function of solution supply velocity, part size, weight, shape and other factors, so that it varied somewhat over the several Examples.

Two different sizes of articles to be plated were utilized, these being (1) rectangular coupons measuring approximately 3 mm. .times. 10 mm. .times. 19 mm. and (2) rectangular blocks measuring 8 mm. .times. 13 mm. .times. 25 mm.

The articles, contained in an open mesh, sieve-like, stainless steel wire basket, were first given the pre-plating treatment hereinbefore described and were then given a strike layer of Ni-B alloy by immersion for about 10 mins. in a 4-liter beaker which contained an electroless Ni-B plating bath (but no diamond particles) of the composition: Nickel acetate .4H.sub.2 O 50 g/l Sodium citrate .2H.sub.2 O 25 g/l Lactic acid 25 g/l Dimethylamine borane (reducing 2.5 g/l agent) Thiodiglycolic acid (stabilizer) 0.1 g/l Santomerse S (comm'l wetting agent) 0.1 g/l NH.sub.4 OH (in quantity required to main- tain pH at 6.5) Water Balance

The strike bath was maintained at a temperature of 55.degree.C. The sample-containing basket was gently agitated. The specimens, plated with a thin nickel strike, were then dumped from the basket into the plating chamber of a tumble plater of the general design described supra through which was flowed the same plating solution as was used for the strike at a rate of approximately 4,200 cm.sup.3 /min. and plating was continued for about 1 hr. before any particulate diamond additions. In Examples 1 through 4, in which 8 and 9.mu. classified size grades of powder (nominal size range 6-12.mu.) were used, the powder added was furnished in amount sufficient to establish a concentration of suspended particles of 2 gm./liter of plating bath. In Example 5, in which a rough 1 to 10.mu. size grade of .alpha.SiC powder was used, the concentration of powder added was increased to 3 gm./liter to establish a concentration of particles in the 6 to 10.mu. size range approximately equivalent to that of Examples 1 through 4. A description of the type powder employed in each Example is reported in Table 2. The period of composite plating was approximately 3.5 hours.

                  Table 2
    ______________________________________
    Description of Powder Added to Tumble Plater
    Example                              Particle
    No.   Type           Structure       Size
    ______________________________________
    1     synthetic   Fine-grained polycrystalline
                                         9
          diamond "A" particles
    2     natural     Single crystal diamond cubic
                                         9
          diamond     (ASTM x-ray data card
                      No. 6-0675)
    3     synthetic   Single crystal diamond cubic
                                         9
          diamond "B" (ASTM x-ray data card
                      No. 6-0675)
    4     .alpha.Al.sub.2 O.sub.3
                      Hexagonal (ASTM x-ray data
                                         8
                      card No. 10-173)
    5     .alpha.SiC (types
                      Hexagonal (ASTM x-ray data
                                         1 to
          I & III     cards No. 2-1463 and 2-1462,
                                         10
          mixed)      respectively)
    ______________________________________


Metallographic examination of the composite coatings obtained in Examples 1-5, inclusive, revealed that they appeared to be nonporous and consisted of a uniform dispersion of the particulate phase in the electroless Ni-B alloy matrix. Quantimet analysis was used in all examples hereinafter described, to determine particulate concentration in the coatings laid down. This employs the Quantimet Image Analyzing Computer marketed by Metals Research, Ltd., Hertz, England, using photomicrographs taken at preselected magnifications which indicated, for Examples 1-5, inclusive, that about 10 vol. per cent of the composite coatings consisted of particles.

The samples were prepared for metallographic examination as follows:

1. The coated surface was ground flat on 600 grit SiC abrasive papers,

2. Rough polishing was then performed with 6-.mu. diamond abrasive on hard-backed Pellon Pan W cloth,

3. Final polishing was then done for a short period with 0.05.mu. Al.sub.2 O.sub.3 abrasive, taking care to avoid grinding through the coating as well as avoiding excessive "rounding", and

4. Photographing at an appropriate magnification for epidiascopic examination using the Quantimet image analyzing system as indicated: Particles <3.mu.-photograph at .about.1500X 3 to 5.mu.-photograph at .about.1000X >6.mu.-photograph at .about.500X

It was practicable to conduct metallographic examinations successfully on wear test samples prepared as hereinafter described, thereby saving double sample preparation.

The as-plated surfaces of the composite coatings were examined with a scanning electron microscope (SEM) at magnifications ranging from 2,000X to 15,000X. Scanning electron photomicrographs, such as FIG. I (6340X), showed the synthetic diamond "A" particles embedded in the composite coatings plated in Example 1 largely by a nucleation mechanism occurring at a number of different sites for each particle. This is unique to diamond "A," as FIG. II for natural diamond and many other photomicrographs (not reproduced here) for synthetic diamond "B" show.

The reason for enhanced nucleation on synthetic diamond "A" is not fully understood; however, the surface topography of diamond "A" is so much rougher than that of natural diamond, and diamond "B," also, that it is believed this has a significant effect. Thus, referring to FIG. I, diamond "A" is seen to have recessed growth ledges (1), craters (2), upstanding growth projections (3) and a multitude of other irregularities which appear to present optimum sites for the nucleation of Ni-B alloy grains (4) on the diamond surface per se. In addition, there exists a complete ring of Ni-B nucleated grains around the edge of the diamond "A" particle. The smooth, quite uniform Ni-B grain matrix existing outwards from the diamond particles is relatively continuous and depressed for all of the diamond particles, regardless of type.

Diamond "A" particles have a fine-grained polycrystalline structure, being made up of a multitude of contiguous diamond crystallites tightly bonded directly to one another in an essentially unoriented pattern. The microstructure of diamond "A" is characterized by a bimodal crystallite size distribution, single coherent particles containing a population of very small, blocky, variously oriented crystallites, typically having diameters in the 10-40 A range, interspersed with much larger blocky, unoriented crystallites, typically having diameters in the 100-1600 A range, and mean diameters in the 200 -600 A range, as described in Belgian Pat. No. 735,374 and Jl. Applied Physics, Vol. 42, pp. 503-510 (1971). The surfaces of these particles are irregular and of relatively large area, e.g., a specific surface area of about 2 sq. meters/gm., ideal for promoting nucleation of the matrix metal thereon.

Nucleation of Ni-B grains on the diamond "A" surfaces is evidence that chemical bonds form between the diamond and the alloy grains. In addition, the Ni-B alloy grains cover all, or at least a major portion of, the diamond surface, including under and around projections, and around ledges, affording enhanced keying retention of the diamond particles in the alloy.

Referring to FIG. II (6480X) for natural diamond, the sparseness of nucleation (3) is clearly apparent, there being only a single small nucleation growth at about 3 o-clock position. Thus, applicants' research has shown that there is little or no nucleation growth with respect to natural diamond and diamond "B," except where the plating bath is on the verge of decomposition, under which conditions the nucleation frequency is greatly enhanced. When a plating bath can be operated under conditions approaching bath decomposition, then plating can nucleate at many sites, even on particles such as natural diamond and diamond "B," as they are incorporated into the coating. (Refer Examples 26, 27, 28.)

Since natural diamond and synthetic diamond "B" both have a single crystal structure, there are few crystal growth defects, such as stacking faults, or macroscopic growth defects, such as ledges or projections. SEM examination of the type represented by FIG. II, reveals that both natural diamond and diamond "B" are characterized by diamond surfaces which appear to be smooth and flat and possessed of few ledge type defects. These smooth surfaces appear to be cleavage planes of the diamond cubic system. Encapsulation of the natural and diamond "B" particles takes place by outward growth of Ni-B alloy grains from the catalytic sites of the original substrate until they overlie the diamond, after which lateral growth of the Ni-B alloy grains proceeds along with continued outward growth. This type of growth can be confirmed, since at times, after diamond laydown, one can, typically, observe, below the level of the growing Ni-B alloy grains, a smooth diamond surface about 1-5.mu. diameter remaining of the original diamond particle expanse of about 9.mu.. This clearly indicates the lateral growth of the Ni-B alloy grains slowly covering the smooth diamond surface simultaneously with the continued outward growth of the Ni-B grains.

Similarly, the typical structures shown in FIG. II for Example 2 has been found to exist also in Ni-P composites incorporating natural diamond particles.

It should be understood that the nucleation and growth of electroless alloy grains on catalytic surfaces is completely different from that occurring with electrodeposited coatings. Since nucleation and growth of metal or metal alloy grains depends, in electroplating, upon the discharge of metal ions at a conductive surface and, since diamond is non-conductive, there can be no chemical bonding, only physical entrapment of diamond in an electrodeposited matrix. In addition, the inclusion of non-conductive diamond particles in an electrodeposited matrix results in shielding of some metallic areas from any applied potential. The shielded areas will either not plate at all, or will at least plate at a slower rate than non-shielded areas, depending upon the degree of shielding, which results in voids in the coating. Voids do not occur in an electroless alloy/non-conductive particle coating as long as there is suitable solution agitation and movement of the article being plated. This movement and agitation affords fresh metallic ions and reducing agent ingress to all surfaces, at the same time voiding gaseous reaction products as deposition proceeds.

An extremely important plating variable which requires control is stabilizer concentration, and this is particularly true for diamond "A" .

In general, the stabilizer concentration must be high enough to prevent spontaneous decomposition of the plating bath as well as prevent nucleation of plating on the surfaces of the diamond particles suspended in the bath. However, if stabilizer concentration is too high, nucleation of plating on the diamond "A" particles that come into contact with, and are incorporated in, the coating being deposited will be stifled. Indeed, excessively high stabilizer concentration poisons the electroless plating reaction completely, even on a metallic surface which is normally a catalyst for electroless plating, preventing the formation of any coating whatever.

Experiments 16, 17, and 18 hereinafter reported, utilizing an electroless Ni-B process stabilized with thiodiglycolic acid (TDGA), show that the nucleation of plating on diamond "A" particles is significantly inhibited at stabilizer concentrations below those which completely poison the plating reaction on the metallic matrix phase. Therefore, to achieve the unique attachment of diamond "A" particles in the plating of electroless composite coatings, the stabilizer concentration must be much more carefully controlled than in conventional electroless plating. It is best practice, in the electroless plating of diamond "A," to determine, by experiment, the optimum stabilizer concentration for each individual plating process a well as for each individual bath stabilizer employed.

Other plating variables which affect the nucleation of plating on all diamond types are pH, bath temperature and reducing agent concentration. For each electroless alloy process, these variables must be carefully controlled to achieve nucleation at multitudinous sites on the diamond particles as these are incorporated into the composite coating while, at the same time, preventing plating on the particles suspended in the bath.

For the electroless Ni-B process of Example 1, the operating temperature limits within which the desired nucleation will occur are relatively broad, ranging from about 50.degree.C. to about 80.degree.C. At a temperature of above about 80.degree.C., plating starts to initiate on the diamond particles suspended in the bath, causing it to decompose. On the other hand, at temperatures below about 50.degree.C. nucleation of plating is substantially inhibited. In addition, the effect of temperature on abrasive wear resistance is shown by Examples 1 and 15. Thus (Example 15), in a highly accelerated yarn line wear test, an electroless Ni-B/9.mu. diamond "A" coating deposited at 40.degree.C. (i.e., 10.degree. below the minimum level for best results), where nucleation on the particles is stifled, had a wear rate of 9.6.mu./hr. A comparable coating plated by the same process at 55.degree.C. (Example 1), where abundant nucleation occurs on the incorporated diamond particles, had a wear rate of only 5.1.mu./hr.

Some of the SiC particles in the coating of Example 5 showed evidence of plating nucleation, but the number of nucleation sites per particle was much less than that on diamond "A," Example 1.

WEAR TESTING

Since one very demanding abrasive service is yarn line processing, two coating wear tests were developed using running yarn lines as the abrading agents, the Standard Test being conducted with dry yarn, whereas the Accelerated Test employed a yarn wet with an abrasive slurry.

The specimens used in these tests consisted of coupons measuring about 0.5 mm. wide cut from plated rectangular blocks measuring about 8 mm. .times. 13 mm. in cross-section.

The procedure (Technique R) utilized for preparation of coated polymer test specimens was as follows:

1. Sample mounted, in duplicate, in "Quick Mount" quick-setting mounting resin,

2. Coated block sectioned with a hack saw perpendicular to the long axis of the specimen,

3. Grind hack-sawed edge successively on 240, 400 and 600 grit SiC abrasive papers, turning the specimen 90.degree. between steps,

4. Rough-polish the hack-sawed edge with 6-.mu. diamond abrasive on a hard-backed Pellon Pan W cloth,

5. Final-polish the hack-sawed edge with 0.05.mu. gamma Al.sub.2 O.sub.3 on a soft Micro-Cloth cloth,

6. Using a hacksaw cut approximately a 1/8 inch slice from this mount parallel to the hack-sawed edge,

7. Mount this 1/8 inch slice on a stainless steel block with two-sided tape, with the previously polished surface next to the block,

8. Grind down outboard face to approximately 22 mils thickness with 240 grit abrasive paper,

9. Repeat steps 3 through 5, bringing to a final thickness of 18-20 mils, and

10. Remove the specimen from the stainless steel block using ethyl alcohol or a similar solvent to soften the tape without damaging the base material, and carefully peel the mounting medium from the test piece.

The procedure (Technique S) utilized for preparation of coated metallic wear test specimens was as follows:

1. Carefully clamp the coated metal specimen in a small, portable, precision vice for sectioning with a wafer machine,

2. Align the vice so that the specimen long axis is perpendicular to the SiC cutting wheel,

3. Slowly cut with two edge cuts to give a 30 mil slice from the block,

4. Follow steps (3)-(5), inclusive, of Technique R for both cut edge surfaces. Final thickness should be 18-20 mils, and

5. Etch in ethyl alcohol plus 4 vol. per cent HNO.sub.3 for 2-5 secs. to delineate the coating-substrate interface.

The front and back surfaces of the test pieces were so smooth and polished that 250X photomicrographs could be taken before and after testing in order to evaluate the amount of wear. Photomicrographs were also taken in plan of the surface of the coatings before and after wear testing to distinguish between a valid test, where the wear track extends across the entire width of the coating, and an invalid test, where corner notching occurring at the front and/or back edges is the result of localized edge cutting and the central part of the wear track remains essentially untouched.

Both Tests employed the same general apparatus, shown schematically in FIGS. IIIA-IIIC, except that only the Accelerated Test used the slurry nozzle denoted at 28.

Test specimens were clamped in position during testing in a holder, not shown, which was provided with sets of vertical ceramic pins in front of and back of the specimen, which pins defined a vertical slot normal to the width of the specimen about 0.25 mm. wide through which the yarn line 29 ran. The yarn is drawn from a bobbin (not shown) on the left side of FIG. IIIA and is trained through "pig tail" ceramic guides 30, through two sets of tensioning disks 31a and 31b, and thence under a 3.2 mm. diameter horizontal ceramic pin 32 located 35 mm. in front of the central axis of the specimen 33. The yarn line next runs across the top coated surface 33a of the specimen and leaves at a slight downward angle by transit under 3.2 mm. diameter horizontal pin 35 located 35 mm. downstream from the central axis of the specimen. The vertical position of the specimen can be adjusted by elevating screws or the like, not shown, to preselect the break angle between running yarn 29 and the horizontal plane of coated surface 33a.

STANDARD WEAR TEST

The Standard Test conditions adopted in Application Ser. No. 103,355 supra were used, these being as follows:

    Yarn:      15-denier monofilament, full dull nylon
                (Code designation 15-1-0-680D)
                (Merge designation 15261)
    Yarn Tension:
               10 gms.
    Yarn Speed:
               1000 yds./min.
    Break Angle:
               5.degree.


Wear Rate in microns per hour was defined as the average depth of the normal wear groove N, i.e., the sum of the wear grooves measured in front, df, and back, db, respectively, divided by 2, the whole divided by the test time in hours, as diagrammed for the lower test track, FIG. IIIE. (Very accurate measurements of the wear tracks were made from leading and trailing side elevation (i.e., edge-on) photomicrographs under high magnification both before and after each wear test.) Under the test conditions described, the electroless Ni-P alloy with 9.mu. diamond "A" composite coatings exhibited surface polishing but no measurable wear even after 8 hours of continuous testing.

Increasing the severity of the test by increasing the tension to 15 gms. and the break angle to 10.degree. did result in some moderate localized edge cutting (M) of the Ni-B, diamond "A" composite coatings after 24 hours continuous testing; however, none of the tests were valid because the central regions under the yarn track were observed to be essentially unmarked (refer upper test track, FIG. IIIE). The notches (M) cut in the edges of the coatings were examined by scanning electron microscopy to ascertain differences in wear mechanisms for comparable electroless alloy composite coatings with different types of diamonds, the results of which are hereinafter reported for individual Examples.

ACCELERATED WEAR TEST

An Accelerated Wear Test in which aqueous slurries of abrasive particles were applied to running yarn line 29 was developed to obtain quantitative wear measurements on our electroless alloy diamond composite coatings. This utilizes a slurry applicator 28 between tensioning disks 31a, 31b and the first ceramic pin 32 as shown in FIG. IIIA, i.e., 14.9 cm. ahead of the center line of specimen surface 33a.

Applicator 28 was provided with an axial bore 28a a measuring 0.508 mm. dia. which opened into a vertical-sided end notch 28b 3.18 mm. long, as measured in a horizontal plane in the direction of yarn line travel. The base surface of notch 28b was a convex arc of radius 1.58 mm. drawn from the vertical axis of the applicator. The upper inner edges of notch 28b were beveled outwardly at slopes of 40.degree. measured from the vertical. The yarn line traversed the orifice 28a diametrically at zero break angle, making essentially tangent contact with the orifice lips. An abrasive slurry of oxide particles dispersed in water was pumped through applicator 28 and metered onto the yarn line. Initial scouting experiments were conducted with slurries of 20 wt. per cent pigmentary TiO.sub.2. Subsequent work indicated that the severity of wear obtained with slurries of 15% Linde A, .alpha.-Al.sub.2 O.sub.3, was much greater. The relative severities of the tests run are compared in Table 3, as to which the material tested was Vasco 7152, a tool steel customarily used in the textile industry for severe abrasive wear applications. Wear rate is expressed in terms of depth of groove cut per unit time, i.e., .mu./hr., into the uncoated steel coupon.

                  Table 3
    ______________________________________
    YARNLINE COMPARATIVE WEAR TEST SEVERITY
    ______________________________________
    Material Tested: Vasco 7152 Tool Steel
    Yarn: 15-denier, monofilament full dull nylon
    Yarn Speed: 1000 yds./min.
    Abrasive Slurry Feed Rate: 2.8 ml./min. for Test No. 3 and
     2.5 ml./min. for Test No. 2.
         Yarn     Yarn
    Test Tension  Break       Abrasive  Wear Rate,
    No.  gms.     Angle (Degs)
                              Slurry    .mu./hr.
    ______________________________________
    1    15       10         None       2.4
    2    10       10         0.7.mu. TiO.sub.2
                                        280
                             in H.sub.2 O (conc'n
                             20 wt. %)
    3    10        5         0.3.mu. Al.sub.2 O.sub.3
                                        1450
                             in H.sub.2 O (conc'n
                             15 wt. %)
    ______________________________________


Under the circumstances, the conditions of test No. 3 were selected for the Accelerated Wear Test for quantitative evaluation of the electroless alloy diamond composite coatings. This test is severe enough to cut grooves, or at least leave visible traces, in diamond composite coatings which extend across the entire width of the test samples, thereby permitting valid quantitative wear rate determination. The test is also severe enough to rapidly cut grooves in high density bult Al.sub.2 O.sub.3.

A comparison of accelerated yarn wear test results for five electroless Ni-B composite coatings containing particles about 9.mu. dia. of Al.sub.2 O.sub.3, SiC and three different types of diamonds, Examples 1-3, respectively, is reported in Table 4. All of the coatings reported were plated by the tumble plating process of appl'n Ser. No. 103,355 supra. Each contained about 10 vol. per cent of the particulate phase dispersed in the electroless Ni-B alloy matrix.

                  Table 4
    ______________________________________
    ACCELERATED YARNLINE WEAR TEST RESULTS
    Test Conditions:
              Same as Test No. 3 in Table No. 3 with a slurry
               feed rate of 2.8 ml./min.
                                Test    Wear
    Example                     Time,   Rate,
    No.        Material         min.    .mu./hr.
    ______________________________________
    1      Electroless Ni-B/9-.mu. Diamond
                                85      5.1
            "A" Composite Coating
    2      Electroless Ni-B/9-.mu. Natural
                                85      10.2
            Diamond Composite Coating
    3      Electroless Ni-B/9-.mu. Diamond
                                85      13.1
            "B" Composite Coating
    --     Bulk 99.5% Al.sub.2 O.sub.3 (Alsimag 785)
                                30      57
    4      Electroless Ni-B/8-.mu. Al.sub.2 O.sub.3
                                 9      109
            Composite Coating
    5      Electroless Ni-B/1-10.mu. SiC
                                 5      278
            Composite Coating
    --     Vasco 7152 Tool Steel
                                20      1,450
    --     Electroless Ni-B As-plated
                                1/30    23,000
            (with no particles)
    ______________________________________


From Table 4 it can be seen that the three electroless Ni-B diamond composite coatings are approximately a factor of 8 to 20 times more wear-resistant than the Ni-B Al.sub.2 O.sub.3 composite coating and approximately a factor of 20-55 times more wear-resistant than the Ni-B(SiC) composite coating. The rate of abrasive wear for the electroless Ni-B 9.mu. diamond "A" is approximately a factor of two less than that of the comparable composites with natural diamond or diamond "B." The superior wear resistance of electroless alloy diamond "A" composite coatings demonstrated is attributable to the strong chemical bond formed between the diamond "A" particles and the electroless alloy matrix due to extensive nucleation of plating on the diamond as hereinbefore described.

The effect of particle size and volume loading on yarnline wear resistance for electroless diamond composite coatings is apparent from Table 5.

                  Table 5
    ______________________________________
    EFFECT OF PARTICLE SIZE AND VOLUME LOADING
    ON YARNLINE WEAR RESISTANCE
    Coating Matrix:
                Electroless Ni-B alloy deposited by
                 process cited in Example 1.
    Dispersed Phase:
                Explosively formed diamond "A".
    Dispersed Phase Data    Wear Test Data
    Example Average Particle
                           Volume,  Time,  Rate,
    No.     Size, .mu.     %        min.   .mu./hr.
    ______________________________________
    23      12-22          16       85     3.4
     1      9              10       85     5.1
    16      5              20       85     6.2
    13      3              29       30     11.6
    11      3               5       10     65
     8      1              20        2     216
    ______________________________________


For the electroless Ni-B composite coatings of Examples 16, 13 and 8 the rate of abrasive wear increases from 6.2.mu./hr. to 216.mu./hr. as the average particle size decreased from 5.mu. to 1.mu.. The wear resistance of the coatings with particles about 3.mu. diameter is very sensitive to volume loading, as indicated for Examples 11 and 13. The yarnline resistance for other types of wear-resistant particles exhibit the same trends (directly proportional to the loadings) with respect to the effects of particle size and volume loading.

Examples 6 and 7

Examples 6 (synthetic diamond "A") and 7 (natural diamond) illustrate the differences in yarnline wear resistance of electroless Ni-P alloy composite coatings containing 1.mu. diamond "A" and 1.mu. natural diamond particles, respectively. In these experiments plain carbon steel blocks were rack-plated in the apparatus of FIG. IX hereinbefore described.

The fifteen steel blocks ranged in size from 6 mm. .times. 10 mm. .times. 15 mm. to 6 mm. .times. 6 mm. .times. 12 mm. These were given the conventional preplating treatment for steel supra. and then immersed for 30 mins. in a Cuposit NL-63 electroless Ni-P plating bath maintained at 85.degree.C. contained in the apparatus 22 cm. dia. jar. The blocks were disposed on lower shelf 12, permitting coating of top and side surfaces; however, only the top coating was wear-tested.

Then a slurry containing a preselected one of the types of particulate diamonds supra in concentration to finally give 4 gms. of powder per liter was slowly added. The stirrer was operated at 350 .+-. 10 rpm to maintain a good powder dispersion in the plating bath and the composite Ni-P alloy-diamond composites were laid down for 3.5 to 4 hrs.

Specimens rack-plated as described contain a higher volume per cent of the diamond particulate phase in the horizontal top surface coating than on the sides, and this was the surface chosen for wear testing because the dispersion was most uniform.

Metallographic examination of the composite coatings of Examples 6 and 7 showed that both possessed a uniform dispersion of diamond particles in the Ni-P alloy matrices. Quantimet analyses of photomicrographs at 1800X showed that the composite coatings contained about 20 volume per cent of particulate diamond.

Results of accelerated yarnline wear tests conducted identically with Examples 1 through 5 supra were as follows:

                  Table 6
    ______________________________________
                                 Test    Wear
    Example                      Time,   Rate,
    No.      Composite Coating   Minutes .mu./hr.
    ______________________________________
    6      Electroless Ni-P/1.mu. diamond "A"
                                 2       378
    7      Electroless Ni-P/1.mu. natural
                                 2       732
           diamond
    ______________________________________


Comparison of Example 6 with Example 7 shows that diamond "A" in Ni-P matrix is superior to natural diamond in the same matrix.

EXAMPLE 8

Fifteen steel blocks were rack-plated with an electroless Ni-B alloy composite coating containing one .mu. diamond "A" by the same technique as employed for Examples 6 and 7, except that an electroless Ni-B bath of the type of Example 1 was used. The blocks were given a strike for 20 mins. before diamond addition.

The particulate diamond "A" (1.mu. size) was slowly added in an amount establishing the final diamond concentration of the bath at 4 gm./liter, and composite plating was conducted at 55.degree.C. for 4 hrs.

Again, metallographic examination of the top horizontal surface of the blocks confirmed that there was a uniform diamond dispersion, and Quantimet analysis indicated a 20 volume per cent diamond loading.

In a 2 minute accelerated wear test, conducted under identical conditions as Examples 1, 6 and 7, the measured wear rate was 216.mu./hr.

It was concluded that the Ni-B composite of Example 8 was appreciably superior to the Ni-P composite of Example 6.

EXAMPLES 9 and 10

These examples illustrate the differences in yarnline wear resistance as a function of diamond type.

Examples 9 and 10 were, respectively, Ni-P alloy/9.mu. diamond "A" and Ni-P alloy/9.mu. natural diamond composites laid down on polymeric substrates.

For each Example, three blocks and five coupons were prepared from ABS polymer, and the same from fiber-reinforced ABS. The blocks measured 8 .times. 13 .times. 25 mm. and the coupons 3 .times. 10 .times. 19 mm. All pieces were tumble-plated as hereinbefore described for Example 1.

All specimens were given the preplating treatment hereinbefore described for ABS resins and were then coated as follows:

1. 10 mins. of electroless Ni-P strike in a Cuposit NL-61 bath maintained at 65.degree.C. in a 4-liter beaker,

2. 60 mins. of tumble plating in a Cuposit NL-61 electroless Ni-P bath maintained at 65.degree.C. in a tumble plater of the general design taught in application Ser. No. 103,355 supra, and

3. 2.5 to 3 hrs. of composite tumble plating in Cuposit NL-61 bath at 65.degree.C. containing a

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Title: Method for concomitant particulate diamond deposition in electroless plating, and the product thereof

Doc Type:
Abstract: This invention is a method for depositing on an article a coating containing at least one member of the group metals and metal alloys plus particulate dispersed diamond comprising contacting the surface of the article with a stable electroless plating bath consisting essentially of an aqueous solution of soluble constituents of the group, electroless reducing agent therefor, a suspension of diamond particles therein and a stabilizer, and maintaining the diamond particles in suspension throughout the bath during the coating of the article for a time sufficient to produce a preselected depth of coating on the article, and the coated article per se.


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Inventors: Christini, Theodore Peter (Kennett Square, PA, US)
Eustice, Albert Lawrence (Wilmington, DE, US)
Graham, Arthur Hughes (Wilmington, DE, US)

Application Number: 341529
Filing Date: 1973-03-15
Publication_date: 1976-02-03
Assignee: E. I. Du Pont de Nemours & Company (Wilmington, DE)
Primary Class(es): 428/614 51/309, 106/1.13, 106/1.22, 427/305, 427/438, 428/323, 428/426, 428/433, 428/545, 428/668, 428/679, 428/684, 428/936
Other Classes:
US Patent Ref:
2858256Oct, 1958Fahnoe et al.51/309.
3061525Jun, 1959Grazen204/9.
3212918Oct, 1965Tsu et al.117/47.
3379556Apr, 1968Chiecchi117/47.
3484282Dec, 1969Gabler et al.117/47.
3617363Nov, 1971Metzger et al.117/130.
3644183Feb, 1972Odekerken117/130.
3674447Jul, 1972Bellis29/196.
3753667Aug, 1973Metzger et al.29/195.

Other Refs: 709,4701,621,206
Jan, 1968BE.
Jun, 1971DT
Other References: Translation of German Offen. 1621206.