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Patent 1339810 Summary

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(12) Patent: (11) CA 1339810
(21) Application Number: 609531
(54) English Title: PROCESS FOR THE PREPARATION OF NOBLE METAL COATED NON-NOBLE METAL SUBSTRATES, COATED MATERIALS PRODUCED IN ACCORDANCE THEREWITH AND COMPOSITIONS UTILIZING THE COATED MATERIALS
(54) French Title: PROCEDE DE PREPARATION DE SUBSTRATS EN METAL NON PRECIEUX REVETUS DE METAL PRECIEUX, MATERIAUX REVETUS AINSI PRODUITS ET COMPOSITIONS UTILISANT DE TELS MATERIAUX
Status: Deemed expired
Bibliographic Data
(52) Canadian Patent Classification (CPC):
  • 31/121
  • 31/156
  • 117/77
  • 117/47.6
(51) International Patent Classification (IPC):
  • H01B 1/02 (2006.01)
  • B22F 1/02 (2006.01)
  • C23C 2/02 (2006.01)
  • C23C 2/04 (2006.01)
  • C23C 16/06 (2006.01)
  • C23C 18/16 (2006.01)
  • C23C 18/42 (2006.01)
  • C23C 28/02 (2006.01)
  • H01B 1/22 (2006.01)
  • H05K 1/09 (2006.01)
  • H05K 3/32 (2006.01)
(72) Inventors :
  • OSTOLSKI, MARIAN J. (United States of America)
(73) Owners :
  • OSTOLSKI, MARIAN J. (United States of America)
(71) Applicants :
  • OSTOLSKI, MARIAN J. (United States of America)
(74) Agent: GOWLING WLG (CANADA) LLP
(74) Associate agent:
(45) Issued: 1998-04-14
(22) Filed Date: 1989-08-28
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
237,898 United States of America 1988-08-29

Abstracts

English Abstract



A multi-coating step immersion coating process for producing
a coating of a noble metal on a non-noble metal substrate,
wherein the noble metal is of a predetermined amount
expressed as a percent of the total weight of coated
product, and wherein the non-noble metal substrate is in the
form of fine particles or a powder is disclosed. The process
also utilizes inter-plating step and post-plating step
rising step sequences which together with the use of the
plurality of coating steps consistently results in high
quality product having a uniform coating, excellent
corrosion resistance and excellent electrical conductivity.
Use of the coated products produced according to the process
in a variety of electrically conductive compositions,
including plastics, adhesives and inks, and in plastic and
resin based electromagnetic shielding materials is also
disclosed.



Claims

Note: Claims are shown in the official language in which they were submitted.


68


THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for plating a coating of a noble metal
onto a non-noble metal substrate material, said process
comprising the steps of:
a) preparing a starter aqueous plating solution
containing an amount of free ions of a noble metal to be
plated out onto said substrate material, said noble metal
being selected from the group consisting of silver, gold,
platinum, palladium, iridium, rhodium, ruthenium and osmium,
such that said amount of free ions of said noble metal is
sufficient to plate an amount of an active, non-noble metal
substrate material, in the form of a powder, with a coating
of from 2 to 60 weight percent, based on the total weight of
a final noble metal-coated active non-noble metal substrate
material product, and such that said amount of free ions of
said noble metal plated onto said active non-noble metal
substrate material is sufficient to at least provide a
coating on the surface of said active non-noble metal
substrate material that completely covers the entire surface
of said active non-noble metal substrate material, leaving no
exposed surface of said active non-noble metal substrate
material, said non-noble metal substrate material being
selected from the group consisting of copper, nickel,
aluminum, titanium, zirconium, vanadium, hafnium, cadmium,
niobium, tantalum, molybdenum, tungsten, gallium, indium,
thallium, and combinations of a first one of said non-noble
metal substrate materials seeded with atoms of a second one
of said non-noble metal substrate materials having a greater
affinity than that of said first non-noble metal substrate
material for said selected noble metal to be plated thereon;
b) dividing said starter plating solution, prepared in
step (a), into a plurality of portions, such that each
portion of said starter plating solution contains a
percentage amount of from less than about 1% to about 85%, by
weight, of the total amount of free ions of noble metal to be
plated out that are contained in said starter plating
solution, the percentage amount that is present in any said

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portion being the same as or different from the percentage
amount present in other of said portions;
c) preparing a plurality of individual plating
solution baths into which said active non-noble metal
substrate material is immersible, by selecting a
concentration of free ions of noble metal for each said
plating solution bath which is to be made from a
corresponding one of said plurality of portions of said
starter plating solution, prepared in step (b), said
concentration of free ions of noble metal for each said
individual plating solution bath being in the range of from
about 0.3 to about 65 grams of free ions of noble metal per
liter of plating solution bath, and making each said
individual plating solution bath by adding water to each
corresponding one of said plurality of portions of said
starter plating solution, to increase the volume thereof ,
such that each one of said plurality of individual plating
solution baths has the concentration of free ions of noble
metal, as selected above therefor;
d) immersing an amount of an active non-noble metal
substrate material to be plated into one of said individual
plating solution baths, prepared in step (c), which is
maintained at a temperature in the range of from about 20 °C
to about 100 °C, such that the temperature of said individual
plating solution bath is inversely related to the oxidation
potential of the non-noble metal substrate material being
plated, to cause said free ions of noble metal to plate-out
onto said substrate material until said one of said
individual plating solution baths is depleted of all but a
trace amount of said free noble metal ions contained therein,
thereby forming an intermediate plated substrate material on
which is plated the fraction of free ions of noble metal
contained in said one of said individual plating solution
baths;
e) separating said intermediate plated substrate
material, prepared in step (d), from the depleted plating
solution bath;



B

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f) rinsing said intermediate plated substrate
material, separated in step (e), at least once with a first
series of water rinses;
g) repeating steps (d), (e), and (f) with the rinsed
intermediate plated substrate material resulting from each
previous sequence of steps (d), (e), and (f), and another one
of said individual plating solution baths, until all of said
individual plating solution baths prepared according to step
(c) have been utilized, the sequence of utilization of said
individual plating solution baths being such that when the
concentration of free noble-metal ions in at least two of
said individual plating solution baths is different, said
individual plating solution baths are successively utilized
in the order of decreasing concentration of free ions of
noble metal therein, and further such that the temperature of
each successively utilized individual plating solution bath
is at least as high as the temperature of the preceding
individual plating solution bath, thereby forming further
intermediate plated substrate materials with each repetition
of the sequence of steps (d), (e) and (f), such that each
successive intermediate plated substrate material is
cumulatively plated with the amounts of free ions of noble
metal contained in each of the plating solution baths into
which the intermediate plated substrate material has been
immersed, thereby ultimately forming a final plated substrate
material, onto which has been plated the total said amount of
free ions of noble metal in said original starter plating
solution;
h) rinsing said final plated substrate material,
prepared in step (g), at least once with a second series of
rinses, including rinses with water, an acid, and an alcohol;
i) further rinsing said final plated substrate
material, as rinsed according to step (h), at least once with
a third series of rinses, including rinses with water, and an
alcohol; and
j) drying said final plated substrate material, as
rinsed according to step (i), to produce a final noble
metal-coated active non-noble metal substrate material product.

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2. The process of claim 1 wherein said noble metal is
selected from the group consisting of silver, gold, and
platinum, and said non-noble metal substrate material is
selected from the group consisting of copper, nickel,
copper-seeded aluminum, titanium, and zirconium.

3. The process of claim 1 wherein the starter aqueous
plating solution is prepared by dissolving an amount of a
compound selected from the group consisting of a cyanide,
chloride, nitrate, and an oxide of the noble metal, in
boiling water, to which has first been added an amount of an
alkali metal cyanide of from about 0to 2.5 times the weight
of the selected noble metal compound, the amount utilized
being determined by the degree of solubility of the noble
metal-containing compound in water, such that the amount of
alkali metal cyanide utilized is sufficient to effect
dissolution of the selected noble metal compound in the
solution to produce the desired amount of free ions of the
noble metal.

4. The process of claim 3 wherein when the noble metal
is gold, supplied in any of the selectable forms of noble
metal compound, the amount of alkali metal cyanide utilized
is zero, and further wherein is added to the boiling water
prior to addition of the gold-containing compound, a mixture
of ammonium chloride, sodium citrate and sodium hypophosphate
in a weight ratio of from about 7.0 - 8.0 : 4.5 - 5.5 : 1,
with the overall amount of mixture added to the water being
such that the weight of sodium hypophosphate in the mixture
is from about 2.0 to 2.5 times the weight of the
gold-containing compound.

5. The process of claim 3 wherein the noble metal
oxide is selected from the group consisting of silver oxide,
gold oxide and platinum mon-, di- and tri-oxide.


72
6. The process of claim 3 wherein the noble metal
cyanide is selected from the group consisting of silver
cyanide, gold cyanide, platinum cyanide, potassium
cyanoaurate, potassium cyanoargentate, potassium
cyanoplatinite, sodium cyanoaurite and sodium cyanoplatinite.

7. The process of claim 3 wherein the noble metal
chloride is selected from the group consisting of silver
chloride, gold chloride, platinum chloride, potassium
chloroaurate, potassium tetra- and hexa-chloroplatinate,
sodium chloroaurate, sodium chloro- and hexachloro-platinate
and sodium chloroplatinite.

8. The process of claim 3 wherein the noble metal
nitrate is selected from the group consisting of silver
nitrate, gold nitrate, potassium nitroplatinite and sodium
nitroplatinite.

9. The process of claim 6 wherein the alkali metal
cyanide is selected from the group consisting of sodium
cyanide and potassium cyanide.

10. The process of claim 1 wherein said powder of
active, non-noble metal substrate material has spherical,
flake-shaped or irregular-shaped particles.

11. The process of claim 10 wherein said powder of
active, non-noble metal substrate material has spherical
particles.

12. The process of claim 10 wherein said spherical
particles have a mean diameter of from 5 to 15 microns.

13. The process of claim 10 wherein the largest
dimension of the flake-shaped and irregular-shaped particles
is 20 microns.

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14. The process of claim 1 wherein the coating of noble
metal plated onto the non-noble metal substrate material is
from 15 to 25 weight percent, based on the total weight of
final noble metal-coated active non-noble metal substrate
material product.

15. The process of claim 1 wherein the starter plating
solution is divided into from 2 to 5 portions.

16. The process of claim 1 wherein a first portion of
the plurality of portions into which said starter plating
solution is divided contains from about 20% to about 85%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; a
second portion of the plurality of portions into which said
starter plating solution is divided contains from about 15%
to about 55%, by weight, of the total amount of free ions of
noble metal to be plated out, contained in said starter
plating solution; where a third portion is utilized, said
third portion contains from about 1% to about 30%, by weight,
of the total amount of free ions of noble metal to be plated
out, contained in said starter plating solution; where a
fourth portion is utilized, said fourth portion contains
from about 0.1% to about 30%, by weight, of the total
amount of free ions of noble metal to be plated out,
contained in said starter plating solution; and where a
fifth or subsequent portion is utilized, each of said fifth
and subsequent portions contains less than about 1%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; such
that the sum of the percentages in all of the portions is
100%.

17. The process of claim 1 wherein the separation of
plated substrate material from a depleted plating solution
bath is by decantation.

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18. The process of claim 1 wherein the first series of
rinses of plated substrate material comprises a sequence of
steps selected from the group consisting of rinsing twice in
succession with cold water; rinsing once with warm water,
followed by rinsing once with hot water; and rinsing twice
in succession with hot water.

19. The process of claim 1 wherein the second series of
rinses of final plated substrate material comprises the
sequence of steps of rinsing once with hot water; rinsing
once with a weak acid; rinsing a second time with hot water;
and rinsing once with an alcohol.

20. The process of claim 19 wherein the weak acid is an
aqueous solution of an acid selected from the group
consisting of glacial acetic acid, dilute hydrochloric acid,
dilute nitric acid, and hydrazine.

21. The process of claim 20 wherein the weak acid is an
aqueous solution of 25% glacial acetic acid.

22. The process of claim 19 wherein the alcohol is a
lower alkanol having from 1 to 4 carbon atoms.

23. The process of claim 22 wherein the lower alkanol is
methanol.

24. The process of claim 1 wherein the second series
of rinse steps is performed in sequence from one to four
times.

25. The process of claim 24 wherein the second series
of rinse steps is performed four times.

26. The process of claim 1 wherein the third series of
rinses of final plated substrate material comprises the
sequence of steps of rinsing from 1 to 3 times in succession
with hot water, followed by rinsing in succession from 1 to
3 times with an alcohol.

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27. The process of claim 26 wherein the alcohol is a
lower alkanol having from 1 to 4 carbon atoms.

28. The process of claim 27 wherein the lower alkanol
is methanol.

29. The process of claim 26 wherein 3 hot water rinses
in succession, followed by 3 alcohol rinses in succession are
performed.

30. The process of claim 29 wherein the alcohol is
methanol.

31. The process of claim 1 wherein drying of the final
plated substrate material is by at least one of the methods
selected from the group consisting of washing with acetone;
washing with methanol; air drying at ambient temperature and
pressure; air drying with hot air; and vacuum drying under
reduced pressure.

32. The process of claim 1 wherein a non-noble metal
substrate which is contaminated with one or more of an outer
oxidized layer; a coating of dirt; and a coating of grease,
all of which reduce the activity and susceptibility of the
non-noble metal to be plated with noble metal ions,
is first cleaned and made active before commencement of
plating by washing with a cleaning and activating solution.

33. The process of claim 32 wherein the cleaning and
activating solution is selected from the group consisting of
a sodium or potassium hydroxide solution and a sodium or
potassium cyanide solution.

34. The process of claim 33 wherein if the cleaning
and activating solution is potassium cyanide solution, the
substrate is first mixed with a liquid detergent before
washing with the solution.


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35. The process of claim 1 further comprising mixing
the active non-noble metal substrate material with a liquid
detergent prior to immersing the substrate material in the
first plating solution bath.

36. The process of claim 1 further comprising the step
of repeating said first series of water rinse steps,
according to step (f), once, after completion of the first
series of rinse steps, which follows immersion of the plated
substrate material in the individual plating solution bath
in which the substrate material is plated with the percentage
of free ions of noble metal cumulatively amounting to at
least 85% of the total amount of free ions of noble metal to
be plated out, with there then remaining at least one more
plating solution bath in which plating of the remaining
percentage of free ions of noble metal onto the substrate
material is completed.

37. The process of claim 33 wherein the cleaning and
activating solution is a sodium or potassium hydroxide
solution which has a concentration of from 0.5 to 1.5
grams/liter.

38. The process of claim 33 wherein the cleaning and
activating solution is a sodium or potassium cyanide solution
which has a concentration of from 50 to 60 grams/liter.

39. The process of claim 1 wherein the non-noble metal
substrate material to be plated is first seeded with atoms of
another non-noble metal onto which the noble metal ions more
readily plate.

40. The process of claim 39 wherein the seeding is
performed by washing the substrate material with a solution
containing free ions of the seeding metal.



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41. The process of claim 40 wherein the free ions of
the seeding metal are supplied by dissolving a salt of the
seeding metal in water and adding ammonium hydroxide and
potassium cyanide thereto to maintain the ions of the seeding
metal free in solution.

42. A process for plating silver onto copper according
to claim 1 wherein said noble metal is silver; said non-noble
metal substrate material is copper powder having spherical
particles with a mean diameter of from 5 to 15 microns; the
weight of coating is from 15 to 60 weight percent, based on
the total weight of a final noble metal-coated non noble
metal substrate material product; said starter plating
solution is divided into 5 portions with 5 said individual
plating solution baths being prepared therefrom, such that
75% to 85% of the total amount of free ions of noble metal to
be plated out is contained in the first individual plating
solution bath; 10% to 20% of the total amount of free ions of
noble metal to be plated out is contained in the second
individual plating solution bath; 1% to 5% of the total
amount of free ions of noble metal to be plated out is
contained in the third individual plating solution bath; and
0.1% to 0.5% of the total amount of free ions of noble metal
to be plated out is contained in each of the fourth and fifth
individual plating solution baths, such that the total of all
percentages of amounts of free ions of noble metal to be
plated out in the 5 baths is 100%; the first individual
plating solution bath is maintained at a temperature of from
about 50 °C to about 80 °C; the second through fifth
individual plating solution baths are maintained at a
temperature of from about 85 °C to about 100 °C; said first
series of water rinse steps is performed once and comprises
the sequence of steps of rinsing once with warm water,
followed by rinsing once with hot water; said second series
of rinse steps is repeated 4 times in succession after
completion of the first series of water rinse steps following
plating in the fifth individual plating solution bath, and
comprises the sequence of steps of rinsing once with hot
water; rinsing once with a 25% glacial acetic acid aqueous


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solution; rinsing a second time with hot water; and rinsing
once with methanol; said third series of rinse steps is
performed once and comprises the sequence of steps of rinsing
3 times with hot water, followed by rinsing 3 times with
methanol; and said process further comprises performing a
second series of rinse steps once, after completion of the
first series of rinse steps which follows after plating in
the third individual plating solution bath.

43. The process according to claim 42 wherein drying of
the final plated substrate material is by air drying at
ambient temperature and pressure.

44. The process according to claim 42 wherein the
weight of coating is from 15.0 to 25.0 weight percent, based
on the total weight of final noble metal coated active
non-noble metal substrate material product.

45. The process according to claim 42 wherein the
weight of coating is 17.6 weight percent, based on the total
weight of final noble metal coated active non-noble metal
substrate material product, and 80% of the total amount of
free ions of noble metal to be plated out is contained in the
first individual plating solution bath; 16% of the total
amount of free ions of noble metal to be placed out is
contained in the second individual plating solution bath;
3.2% of the total amount of free ions of noble metal to be
plated out is contained in the third individual plating
solution bath; and 0.4% of the total amount of free ions of
noble metal to be plated out is contained in each of the
fourth and fifth individual plating solution baths.

46. A process for plating silver onto nickel according
to claim 1 wherein said noble metal is silver; said non-noble
metal substrate material is nickel powder having spherical
particles with a mean diameter of from 5 to 15 microns; the
weight of coating is from 15 to 60 weight percent, based on
the total weight of final noble metal coated active non-noble
metal substrate material product; said starter plating

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solution is divided into 4 equal portions with 4 said
individual plating solution baths being prepared therefrom,
such that 25% of the total amount of free ions of noble metal
to be plated out is contained in each individual plating
solution bath; the first individual plating solution bath is
maintained at a temperature of from about 50 °C to about 80
°C; the second through fourth individual plating solution
baths are maintained at a temperature of from about 85 °C to
about 100 °C; said first series of water rinse steps
comprises the sequence of steps of rinsing twice with hot
water; said second series of rinse steps is repeated 4 times
in succession after completion of said first series of water
rinse steps following plating in the fourth individual
plating solution bath, and comprises the sequence of steps of
rinsing once with hot water; rinsing once with a 25% glacial
acetic acid aqueous solution; rinsing a second time with hot
water; and rinsing once with methanol; said third series of
rinse steps is performed once and comprises the sequence of
steps of rinsing 3 times with hot water, followed by rinsing
3 times with methanol; and said process further comprises
cleaning and activating said nickel powder substrate material
prior to its immersion in the first individual plating
solution bath.

47. The process of claim 46 wherein cleaning and
activation of the nickel powder comprises the steps of first
mixing the nickel powder with liquid detergent to form a
paste; mixing the nickel powder paste with a potassium
cyanide activation solution; separating the cleaned and
activated nickel powder from the activation solution; washing
the activated nickel powder twice with hot water; and
remixing the cleaned and activated nickel powder with liquid
detergent.

48. The process of claim 46 wherein drying of the final
plated substrate material is by air drying at ambient
temperature and pressure.



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49. The process of claim 46 wherein the weight of
coating is from 15.0 to 25.0 weight percent, based on the
total weight of final noble metal-coated active non-noble
metal substrate material product.

50. The process of claim 46 wherein the weight of
coating is 16.0 weight percent, based on the total weight of
final noble metal-coated active non-noble metal substrate
material product; said first individual plating solution bath
is maintained at a temperature of about 75 °C; and said
second through fourth individual plating solution baths are
maintained at a temperature of about 100 °C.

51. A process for plating silver onto aluminum seeded
with copper according to claim 1, wherein said noble metal is
silver; said non-noble metal substrate material is aluminum
powder having spherical particles with a mean diameter of
from 5 to 15 microns, and which have been seeded with copper
atoms; the weight of coating is from 15 to 60 weight percent,
based on the total weight of final noble metal-coated
non-noble metal active substrate material product; said starter
plating solution is divided into 2 equal portions with 2 said
individual plating solution baths being prepared therefrom,
such that 50% of the total amount of free ions of noble metal
to be plated out is contained in each individual plating
solution bath; the first individual plating solution bath is
maintained at a temperature of from about 25 °C to about 35
°C; the second individual plating solution bath is maintained
at a temperature of from about 60 °C to about 70 °C; said
first series of water rinse steps is performed once and
comprises rinsing twice in succession with cold water; said
second series of rinse steps is repeated 4 times in
succession after completion of said first series of rinse
steps following plating in the second individual plating
solution bath, and comprises the sequence of steps of rinsing
once with hot water; rinsing once with a 25% glacial acetic
acid aqueous solution; rinsing a second time with hot water;
and rinsing once with methanol; said third series of rinse
steps is performed once and comprises the sequence of steps


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of rinsing 3 times with hot water, followed by rinsing 3
times with methanol; and said process further comprises the
initial steps, all performed before the first plating step,
of cleaning and activating the aluminum powder; seeding the
aluminum powder with copper atoms; and mixing the
copper-seeded aluminum powder with liquid detergent.

52. The process of claim 51 wherein cleaning and
activation of the aluminum powder comprises the step of
washing it with a sodium or potassium hydroxide solution.

53. The process of claim 52 wherein the sodium or
potassium hydroxide solution has a concentration of from 0.5
to 1.5 grams/liter.

54. The process of claim 51 wherein the initial step of
seeding aluminum powder with copper atoms is performed by
immersing the aluminum powder in a solution containing free
copper ions.

55. The process of claim 54 wherein the solution
containing free copper ions is an aqueous copper sulfate
solution.

56. The process of claim 55 wherein the copper sulfate
solution has a concentration of from 200 to 250 grams/gallon.

57. The process of claim 56 wherein the solution
further contains ammonium hydroxide and sodium or potassium
cyanide.

58. The process of claim 57 wherein ammonium hydroxide
is added to the aqueous copper sulfate solution in the amount
of 300 milliliters/gram.

59. The process of claim 57 wherein sodium or potassium
cyanide is added as aqueous sodium or potassium cyanide
solution having a concentration of from 170 to 180
grams/liter.



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60. The process of claim 51 wherein drying of the final
plated substrate material is by air drying at ambient
temperature and pressure.

61. The process of claim 54 wherein the weight of
coating is from 15.0 to 25.0 weight percent, based on the
total weight of final noble metal-coated active non-noble
metal substrate material product.

62. The process of claim 54 wherein the weight of
coating is 20.3 weight percent, based on the total weight of
final noble metal-coated active non-noble metal substrate
material product; said first individual plating solution bath
is maintained at a temperature of about 32 °C; and said
second individual plating solution bath is maintained at a
temperature of about 65 °C.

63. A process for plating gold onto nickel according to
claim 4, wherein said noble metal is gold; the source of the
free ions of the gold is potassium gold cyanide; said
non-noble metal substrate material is nickel powder having
spherical particles with a mean diameter of from 8 to 10
microns; the weight of coating is from 15 to 60 weight
percent, based on the total weight of final noble
metal-coated active non-noble metal substrate material product;
said starter plating solution is divided into 4 equal
portions with 4 said individual plating solution baths being
prepared therefrom, such that 25% of the total amount of free
ions of noble metal to be plated out is contained in the
first individual plating solution bath; 10% to 20% of the
total amount of free ions of noble metal to be plated out is
contained in each individual plating solution bath; the first
individual plating solution bath is maintained at a
temperature of from about 50 °C to about 80 °C; the second
through fourth individual plating solution baths are
maintained at a temperature of from about 85 °C to about 100
°C; said first series of water rinse steps comprises the
sequence of steps of rinsing twice with hot water; said
second series of rinse steps is repeated 4 times in

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succession after completion of said first series of water
rinse steps following plating in the fourth individual
plating solution bath, and comprises the sequence of steps of
rinsing once with hot water; rinsing once with a 25% glacial
acetic acid aqueous solution; rinsing a second time with hot
water; and rinsing once with methanol; said third series of
rinse steps is performed once and comprises the sequence of
steps of rinsing 3 times with hot water, followed by rinsing
3 times with methanol; and the process further comprises
cleaning and activating the nickel powder substrate material
prior to its immersion in said first individual plating
solution bath.

64. The process of claim 63 wherein cleaning and
activation of the nickel powder comprises the steps of first
mixing the nickel powder with liquid detergent to form a
paste; mixing the nickel powder paste with a sodium or
potassium cyanide activation solution; separating the cleaned
and activated nickel powder from the activation solution;
washing the activated nickel powder twice with hot water; and
remixing the cleaned and activated nickel powder with liquid
detergent.

65. The process of claim 63 wherein drying of the final
plated substrate material is by air drying at ambient
temperature and
pressure.

66. The process of claim 63 wherein the weight of
coating is from 15.0 to 25.0 weight percent, based on the
total weight of final noble metal-coated active non-noble
metal substrate material product.

67. The process of claim 63 wherein the weight of
coating is 16.0 weight percent, based on the total weight of
final noble metal-coated active non-noble metal substrate
material product; said first individual plating solution bath
is maintained at a temperature of about 75 °C; and said
second through fourth individual plating solution baths are
B

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maintained at a temperature of from about 94 °C to about 98
°C.

68. A composition comprising a noble metal plated onto
a non-noble metal substrate material, wherein:
said noble metal is selected from the group consisting
of silver, gold, platinum, palladium, iridium, rhodium,
ruthenium and osmium;
said non-noble metal substrate material is selected from
the group consisting of copper, nickel, aluminum, titanium,
zirconium, vanadium, hafnium, cadmium, niobium, tantalum,
molybdenum, tungsten, gallium, indium, and thallium;
said noble metal is present in said composition in an
amount of from about 2 percent by weight to about 60 percent
by weight; and
said non-noble metal substrate material is a powder
having an outer surface area;
such that said noble metal in said composition is
sufficient to at least completely coat said outer surface
area of said non-noble metal substrate material, leaving no
uncoated, exposed surface area.

69. The composition according to claim 68 wherein said
non-noble metal substrate material powder has spherical,
flake-shaped, or irregular-shaped particles.

70. The composition according to claim 69 wherein said
particles of said non-noble metal substrate material powder
have a mean diameter of from about 5 microns to about 15
microns.

71. The composition according to claim 68 wherein said
noble metal is present in said composition in an amount of
from about 15 percent by weight to about 25 percent by
weight.

72. The composition according to claim 68 wherein said
noble metal is silver and said non-noble metal substrate
material is copper.

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73. The composition according to claim 68 wherein said
noble metal is silver and said non-noble metal substrate
material is nickel.

74. The composition according to claim 68 wherein said
noble metal is gold and said non-noble metal substrate
material is nickel.

75. A composition comprising a noble metal plated onto
a non-noble metal substrate material, wherein:
said noble metal is selected from the group consisting
of silver, gold, platinum, palladium, iridium, rhodium,
ruthenium and osmium;
said non-noble metal substrate material is selected from
the group consisting of copper, nickel, aluminum, titanium,
zirconium, vanadium, hafnium, cadmium, niobium, tantalum,
molybdenum, tungsten, gallium, indium, and thallium;
said noble metal is present in said composition in an
amount of from about 2 percent by weight to about 60 percent
by weight;
said non-noble metal substrate material is a powder
having an outer surface area;
such that said noble metal present in said composition
is sufficient to at least completely coat said outer surface
area of said non-noble metal substrate material, leaving no
uncoated, exposed surface area;
and wherein said composition is produced by a process
comprising:
a) preparing a starter aqueous plating solution
containing an amount of free ions of a noble metal to be
plated out onto said non-noble metal substrate material,
such that said amount of free ions of said noble metal is
sufficient to plate said non-noble metal substrate material
with a coating of from 2 to 60 weight percent, based on the
total weight of a final noble metal-coated non-noble metal
substrate material product, and such that said amount of free
ions of said noble metal plated onto said non-noble metal
substrate material is sufficient to at least provide a
coating on the surface of said non-noble metal substrate


- 86 -

material that completely covers the entire surface of said
non-noble metal substrate material, leaving no exposed
surface of said non-noble metal substrate material;
b) dividing said starter plating solution, prepared in
(a), into a plurality of portions, such that each portion of
said starter plating solution contains a percentage amount of
from less than about 1% to about 85%, by weight, of the total
amount of free ions of noble metal to be plated out that are
contained in said starter plating solution, the percentage
amount that is present in any said portion being the same as
or different from the percentage amount present in other of
said portions;
c) preparing a plurality of individual plating
solution baths into which said non-noble metal substrate
material is immersible, by selecting a concentration of free
ions of noble metal for each said plating solution bath which
is to be made from a corresponding one of said plurality of
portions of said starter plating solution, prepared in (b),
said concentration of free ions of noble metal for each said
individual plating solution bath being in the range of from
about 0.3 to about 65 grams of free ions of noble metal per
liter of plating solution bath, and making each said
individual plating solution bath by adding water to each
corresponding one of said plurality of portions of said
starter plating solution, to increase the volume thereof,
such that each one of said plurality of individual plating
solution baths has the concentration of free ions of noble
metal, as selected above therefor;
d) immersing an amount of a non-noble metal substrate
material to be plated into one of said individual plating
solution baths, prepared in (c), which is maintained at a
temperature in the range of from about 20 °C to about 100 °C,
such that the temperature of said individual plating solution
bath is inversely related to the oxidation potential of the
non-noble metal substrate material being plated, to cause
said free ions of noble metal to plate-out onto said
substrate material until said one of said individual plating
solution baths is depleted of all but a trace amount of said
free noble metal ions contained therein, thereby forming an

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intermediate plated substrate material on which is plated the
fraction of free ions of noble metal contained in said one of
said individual plating solution baths;
e) separating said intermediate plated substrate
material, prepared in (d), from the depleted plating solution
bath;
f) rinsing said intermediate plated substrate
material, separated in (e), at least once with a first series
of water rinses;
g) repeating (d), (e), and (f) with the rinsed
intermediate plated substrate material resulting from each
previous sequence of (d), (e), and (f), and another one of
said individual plating solution baths, until all of said
individual plating solution baths prepared according to (c)
have been utilized, the sequence of utilization of said
individual plating solution baths being such that when the
concentration of free noble-metal ions in at least two of
said individual plating solution baths is different, said
individual plating solution baths are successively utilized
in the order of decreasing concentration of free ions of
noble metal therein, and further such that the temperature of
each successively utilized individual plating solution bath
is at least as high as the temperature of the preceding
individual plating solution bath, thereby forming further
intermediate plated substrate materials with each repetition
of the sequence of (d), (e) and (f), such that each
successive intermediate plated substrate material is
cumulatively plated with the amounts of free ions of noble
metal contained in each of the plating solution baths into
which the intermediate plated substrate material has been
immersed, thereby ultimately forming a final plated substrate
material, onto which has been plated the total said amount of
free ions of noble metal in said original starter plating
solution;
h) rinsing said final plated substrate material,
prepared in (g), at least once with a second series of
rinses, including rinses with water, an acid, and an alcohol;
i) further rinsing said final plated substrate
material, as rinsed according to (h), at least once with a


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third series of rinses, including rinses with water, and an
alcohol; and
j) drying said final plated substrate material, as
rinsed according to (i), to produce a final noble
metal-coated non-noble metal substrate material product.

76. The composition according to claim 75 wherein a
first portion of the plurality of portions into which said
starter plating solution is divided contains from about 20%
to about 85%, by weight, of the total amount of free ions of
noble metal to be plated out, contained in said starter
plating solution; a second portion of the plurality of
portions into which said starter plating solution is divided
contains from about 15% to about 55%, by weight, of the total
amount of free ions of noble metal to be plated out,
contained in said starter plating solution; where a third
portion is utilized, said third portion contains from about
1% to about 30%, by weight, of the total amount of free ions
of noble metal to be plated out, contained in said starter
plating solution; where a fourth portion is utilized, said
fourth portion contains from about 0.1% to about 30%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; and
where a fifth or subsequent portion is utilized, each of said
fifth and subsequent portions contains less than about 1%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; such
that the sum of the percentages in all of the portions is
100%.

77. The composition according to claim 75 wherein said
process further comprises repeating said first series of
water rinses, according to (f), once, after completion of the
first series of rinses, which follows immersion of the plated
substrate material in the individual plating solution bath in
which the substrate material is plated with the percentage of
free ions of noble metal cumulatively amounting to at least
85% of the total amount of free ions of noble metal to be
plated out, with there then remaining at least one more





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plating solution bath in which plating of the remaining
percentage of free ions of noble metal onto the substrate
material is completed.

78. A silver-plated copper powder produced according to
claim 77 wherein said noble metal is silver; said non-noble
metal substrate material is copper powder having spherical
particles with a mean diameter of from 5 to 15 microns; the
weight of silver coating plated onto said copper powder is
from 15 to 60 weight percent, based on the total weight of
final noble metal-coated non noble metal substrate material
product; said starter plating solution is divided into 5
portions with 5 said individual plating solution baths being
prepared therefrom, such that from about 75% to about 85% of
the total amount of free ions of noble metal to be plated out
onto said substrate is contained in the first individual
plating solution bath; from about 10% to about 20% of the
total amount of free ions of noble metal to be plated out
onto said substrate is contained in the second individual
plating solution bath; from about 1% to about 5% of the total
amount of free ions of noble metal to be plated out onto said
substrate is contained in the third individual plating
solution bath; and from about 0.1% to about 0.5% of the total
amount of free ions of noble metal to be plated out onto said
substrate is contained in each of the fourth and fifth
individual plating solution baths, such that the total of all
percentages of amounts of free ions of noble metal to be
plated out in the 5 baths is 100%; the first individual
plating solution bath is maintained at a temperature of from
about 50 °C to about 80 °C; the second through fifth
individual plating solution baths are maintained at a
temperature of from about 85 °C to about 100 °C ; said first
series of water rinses is performed once and comprises the
sequence of rinsing once with warm water, followed by rinsing
once with hot water; said second series of rinses is repeated
4 times in succession after completion of the first series of
water rinses following plating in the fifth individual
plating solution bath, with each repetition comprising the
four-part sequence of rinsing once with hot water, rinsing


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once with a 25% glacial acetic acid aqueous solution, rinsing
a second time with hot water, and rinsing once with methanol;
said third series of rinses is performed once immediately
after completion of the final repetition of said second
series of rinses and comprises the sequence of rinsing 3
times with hot water, followed by rinsing 3 times with
methanol; and said process further comprises performing the
four-part sequence of said second series of rinses once,
after completion of the first series of rinses which follows
after plating in the third individual plating solution
bath.

79. The silver-plated copper powder according to claim
78 wherein the weight of silver plating coated onto said
copper powder is from 15.0 to 25.0 weight percent, based on
the total weight of final noble metal coated non-noble metal
substrate material product.

80. The silver-plated copper powder according to claim
78 wherein the weight of silver plating coated onto said
copper powder is 17.6 weight percent, based on the total
weight of final noble metal coated non-noble metal substrate
material product, and 80% of the total amount of free ions of
silver to be plated out onto said copper powder is contained
in the first individual plating solution bath; 16% of the
total amount of free ions of silver to be plated out onto
said copper powder is contained in the second individual
plating solution bath; 3.2% of the total amount of free ions
of silver to be plated out onto said copper powder is
contained in the third individual plating solution bath; and
0.4% of the total amount of free ions of silver to be plated
out onto said copper powder is contained in each of the
fourth and fifth individual plating solution baths.

81. A silver-plated nickel powder produced according to
claim 75 wherein said noble metal is silver; said non-noble
metal substrate material is nickel powder having spherical
particles with a mean diameter of from 5 to 15 microns; the
weight of silver coating plated onto said nickel powder is

- 91 -
from 15 to 60 weight percent, based on the total weight of
final noble metal coated non-noble metal substrate material
product; said starter plating solution is divided into 4
equal portions with 4 said individual plating solution baths
being prepared therefrom, such that 25% of the total amount
of free ions of noble metal to be plated out is contained in
each individual plating solution bath; the first individual
plating solution bath is maintained at a temperature of from
about 50 °C to about 80 °C; the second through fourth
individual plating solution baths are maintained at a
temperature of from about 85 °C to about 100 °C; said first
series of water rinses comprises the sequence of rinsing
twice with hot water; said second series of rinses is
repeated 4 times in succession after completion of said first
series of water rinses following plating in the fourth
individual plating solution bath, and comprises the sequence
of rinsing once with hot water; rinsing once with a 25%
glacial acetic acid aqueous solution; rinsing a second time
with hot water; and rinsing once with methanol; said third
series of rinses. is performed once and comprises the sequence
of rinsing 3 times with hot water, followed by rinsing 3
times with methanol; and said process further comprises
cleaning and activating said nickel powder substrate material
prior to its immersion in the first individual plating
solution bath.

82. The silver-plated nickel powder according to claim
81 wherein the weight of silver plating coated onto said
nickel powder is from 15.0 to 25.0 weight percent, based on
the total weight of final noble metal-coated non-noble metal
substrate material product.

83. The silver-plated nickel powder according to claim
81 wherein the weight of silver plating coated onto said
nickel powder is 16.0 weight percent, based on the total
weight of final noble metal-coated non-noble metal substrate
material product; said first individual plating solution bath
is maintained at a temperature of about 75 °C; and said


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second through fourth individual plating solution baths are
maintained at a temperature of about 100 °C.

84. A gold-plated nickel powder produced according to
claim 75 wherein said noble metal is gold; said non-noble
metal substrate material is nickel powder having spherical
particles with a mean diameter of from 5 to 15 microns; the
weight of gold coating plated onto said nickel powder is from
15 to 60 weight percent, based on the total weight of final
noble metal coated non-noble metal substrate material
product; said starter plating solution is divided into 4
equal portions with 4 said individual plating solution baths
being prepared therefrom, such that 25% of the total amount
of free ions of noble metal to be plated out is contained in
each individual plating solution bath; the first individual
plating solution bath is maintained at a temperature of from
about 50 °C to about 80 °C; the second through fourth
individual plating solution baths are maintained at a
temperature of from about 85 °C to about 100 °C; said first
series of water rinses comprises the sequence of rinsing
twice with hot water; said second series of rinses is
repeated 4 times in succession after completion of said first
series of water rinses following plating in the fourth
individual plating solution bath, and comprises the sequence
of rinsing once with hot water; rinsing once with a 25%
glacial acetic acid aqueous solution; rinsing a second time
with hot water; and rinsing once with methanol; said third
series of rinses is performed once and comprises the sequence
of rinsing 3 times with hot water, followed by rinsing 3
times with methanol; and said process further comprises
cleaning and activating said nickel powder substrate material
prior to its immersion in the first individual plating
solution bath.

85. The gold-plated nickel powder according to claim 84
wherein the weight of gold plating coated onto said nickel
powder is from 15.0 to 25.0 weight percent, based on the
total weight of final noble metal-coated non-noble metal
substrate material product.

- 93 -
86. The gold-plated nickel powder according to claim 84
wherein the weight of gold plating coated onto said nickel
powder is 16.0 weight percent, based on the total weight of
final noble metal-coated non-noble metal substrate material
product; said first individual plating solution bath is
maintained at a temperature of about 75 °C; and said second
through fourth individual plating solution baths are
maintained at a temperature of about 100 °C.

87. An electrically conductive composition comprising
a noble metal-coated, non-noble metal substrate material
powder, wherein said noble metal is selected from the group
consisting of silver, gold, and platinum, said non-noble
metal substrate material powder is selected from the group
consisting of copper, nickel, aluminum, titanium, zirconium,
vanadium, hafnium, cadmium, niobium, tantalum, molybdenum,
tungsten, gallium, indium, and thallium; such that individual
particles of said non-noble metal substrate material powder
have a mean diameter of from about 5 microns to about 15
microns, and an outer surface area, with said non-noble metal
substrate material powder being coated with said noble metal,
such that said noble metal is in an amount of from about 2
percent by weight to about 60 percent by weight, based on the
total weight of the composition, and further such that said
noble metal in said composition is present in an amount
sufficient to at least completely coat said outer surface
area of said non-noble metal substrate material powder,
leaving no exposed outer surface area of said non-noble metal
substrate material powder uncoated with said noble metal.

88. A composition comprising a noble metal plated onto
a non-noble metal substrate material, wherein:
said noble metal is selected from the group consisting
of silver, gold, platinum, palladium, iridium, rhodium,
ruthenium, and osmium;
said non-noble metal substrate material is a first
non-noble metal selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,

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indium, and thallium, seeded with atoms of a second non-noble
metal selected from the group consisting of copper, nickel,
aluminum, titanium, zirconium, vanadium, hafnium, cadmium,
niobium, tantalum, molybdenum, tungsten, gallium, indium, and
thallium, such that said first non-noble metal and said
second non-noble metal of said non-noble metal substrate
material are different and further such that said noble metal
has a greater affinity for plating-out onto said second
non-noble metal than for plating-out onto said first non-noble
metal;
said noble metal is present in said composition in an
amount of from about 2 percent by weight to about 60 percent
by weight, based on the total weight of the composition; and
said non-noble metal substrate material is a powder
having an outer surface area;
such that said noble metal in said composition is
sufficient to at least completely coat said outer surface
area of said non-noble metal substrate material, leaving no
uncoated, exposed surface area.

89. The composition according to claim 88 wherein said
non-noble metal substrate material powder has spherical,
flake-shaped, or irregular-shaped particles.

90. The composition according to claim 89 wherein said
non-noble metal substrate material powder has spherical
particles.

91. The composition according to claim 89 wherein said
particles of said non-noble metal substrate material powder
have a mean diameter of from about 5 microns to about 15
microns.

92. The composition according to claim 88 wherein said
noble metal is present in said composition in an amount of
from about 15 percent by weight to about 25 percent by
weight.




.

-95-

93. The composition according to claim 88 wherein said
noble metal is silver, said first non-noble metal of said
non-noble metal substrate material is aluminum, and said
second non-noble metal of said non-noble metal substrate
material is copper.

94. The composition according to claim 88 wherein said
noble metal is gold and said first non-noble metal of said
non-noble metal substrate material is aluminum, and said
second non-noble metal of said non-noble metal substrate
material is copper.

95. The composition according to claim 88 wherein said
noble metal is platinum and said first non-noble metal of
said non-noble metal substrate material is aluminum, and said
second non-noble metal of said non-noble metal substrate
material is copper.

96. A composition comprising a noble metal plated onto
a non-noble metal substrate material, wherein:
said noble metal is selected from the group consisting
of silver, gold, platinum, palladium, iridium, rhodium,
ruthenium and osmium;
said non-noble metal substrate material is a first
non-noble metal selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, and thallium, seeded with atoms of a second non-noble
metal selected from the group consisting of copper, nickel,
aluminum, titanium, zirconium, vanadium, hafnium, cadmium,
niobium, tantalum, molybdenum, tungsten, gallium, indium, and
thallium, such that said first non-noble metal and said
second non-noble metal of said non-noble metal substrate
material are different and further such that said noble metal
has a greater affinity for plating-out onto said second
non-noble metal than for plating-out onto said first non-noble
metal;


-96-

said noble metal is present in said composition in an
amount of from about 2 percent by weight to about 60 percent
by weight;
said non-noble metal substrate material is a powder
having an outer surface area;
such that said noble metal present in said composition
is sufficient to at least completely coat said outer surface
area of said non-noble metal substrate material, leaving no
uncoated, exposed surface area;
and wherein said composition is formed by the process
of:
a) seeding said first non-noble metal of said
substrate material with atoms of said second non-noble metal
of said substrate material;
b) preparing a starter aqueous plating solution
containing an amount of free ions of a noble metal to be
plated out onto said non-noble metal substrate material,
such that said amount of free ions of said noble metal is
sufficient to plate said non-noble metal substrate material
with a coating of from 2 to 60 weight percent, based on the
total weight of a final noble metal-coated active non-noble
metal substrate material product, and such that said amount
of free ions of said noble metal plated onto said active
non-noble metal substrate material is sufficient to at least
provide a coating on the surface of said active non-noble
metal substrate material that completely covers the entire
surface of said active non-noble metal substrate material,
leaving no exposed surface of said active non-noble metal
substrate material, and combinations of a first one of said
non-noble metal substrate materials seeded with atoms of a
second one of said non-noble metal substrate materials having
a greater affinity than that of said first non-noble metal
substrate material for said selected noble metal to be plated
thereon;
c) dividing said starter plating solution, prepared in
(b), into a plurality of portions, such that each portion of
said starter plating solution contains a percentage amount of
from less than about 1% to about 85%, by weight, of the total
amount of free ions of noble metal to be plated out that are

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contained in said starter plating solution, the percentage
amount that is present in any said portion being the same as
or different from the percentage amount present in other of
said portions;
d) preparing a plurality of individual plating
solution baths into which said active non-noble metal
substrate material is immersible, by selecting a
concentration of free ions of noble metal for each said
plating solution bath which is to be made from a
corresponding one of said plurality of portions of said
starter plating solution, prepared in (c), said concentration
of free ions of noble metal for each said individual plating
solution bath being in the range of from about 0.3 to about
65 grams of free ions of noble metal per liter of plating
solution bath, and making each said individual plating
solution bath by adding water to each corresponding one of
said plurality of portions of said starter plating solution,
to increase the volume thereof, such that each one of said
plurality of individual plating solution baths has the
concentration of free ions of noble metal, as selected above
therefor;
e) immersing an amount of said active non-noble metal
substrate material of a first noble metal seeded with atoms
of a second noble metal, which non-noble metal substrate
material is to be plated, into one of said individual plating
solution baths, prepared in (d), which is maintained at a
temperature in the range of from about 20 °C to about 100 °C,
to cause said free ions of noble metal to plate-out onto said
substrate material until said one of said individual plating
solution baths is depleted of all but a trace amount of said
free noble metal ions contained therein, thereby forming an
intermediate plated substrate material on which is plated the
fraction of free ions of noble metal contained in said one of
said individual plating solution baths;
f) separating said intermediate plated substrate
material, prepared in (e), from the depleted plating solution
bath;
g) rinsing said intermediate plated substrate
material, separated in (f), at least once with a first series

-98-
of water rinses wherein each series of rinses includes a
sequence of steps selected from the group (i - iii)
consisting of (i) rinsing twice in succession with cold
water, (ii) rinsing once with warm water, followed by rinsing
once with hot water, and (iii) rinsing twice in succession
with hot water;
h) repeating (e), (f), and (g) with the rinsed
intermediate plated substrate material resulting from each
previous sequence of (e), (f), and (g), and another one of
said individual plating solution baths, until all of said
individual plating solution baths prepared according to (d)
have been utilized, the sequence of utilization of said
individual plating solution baths being such that when the
concentration of free noble-metal ions in at least two of
said individual plating solution baths is different, said
individual plating solution baths are successively utilized
in the order of decreasing concentration of free ions of
noble metal therein, and further such that the temperature of
each successively utilized individual plating solution bath
is at least as high as the temperature of the preceding
individual plating solution bath, thereby forming further
intermediate plated substrate materials with each repetition
of the sequence or (e), (f) and (g), such that each
successive intermediate plated substrate material is
cumulatively plated with the amounts of free ions of noble
metal contained in each of the plating solution baths into
which the intermediate plated substrate material has been
immersed, thereby ultimately forming a final plated substrate
material, onto which has been plated the total said amount of
free ions of noble metal in said original starter plating
solution;
i) rinsing said final plated substrate material,
prepared in (h), at least once with a second series of
rinses, wherein each of said second series of rinses includes
successive rinses with water, an acid, and an alcohol;
j) further rinsing said final plated substrate
material, as rinsed according to (i), at least once with a
third series of rinses, wherein each of said third series of
rinses includes from 1 to 3 successive rinses with hot water,

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followed by from 1 to 3 successive rinses with an alcohol;
and
k) drying said final plated substrate material, as
rinsed according to (j), to produce a final noble metal-coated
active non-noble metal substrate material product.

97. The composition according to claim 96 wherein a
first portion of the plurality of portions into which said
starter plating solution is divided contains from about 20%
to about 85%, by weight, of the total amount of free ions of
noble metal to be plated out, contained in said starter
plating solution; a second portion of the plurality of
portions into which said starter plating solution is divided
contains from about 15% to about 55%, by weight, of the total
amount of free ions of noble metal to be plated out,
contained in said starter plating solution; where a third
portion is utilized, said third portion contains from about
1% to about 30%, by weight, of the total amount of free ions
of noble metal to be plated out, contained in said starter
plating solution; where a fourth portion is utilized, said
fourth portion contains from about 0.1% to about 30%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; and
where a fifth or subsequent portion is utilized, each of said
fifth and subsequent portions contains less than about 1%, by
weight, of the total amount of free ions of noble metal to be
plated out, contained in said starter plating solution; such
that the sum of the percentages in all of the portions is
100%.

98. A composition according to claim 97 wherein said
starter plating solution is divided into two portions, each
of which contains 50%, by weight, of the total amount of free
ions of noble metal to be plated out, contained in said
starter plating solution.

- 100 -

99. A composition according to claim 96 wherein when
said first non-noble metal of said non-noble metal substrate
material is aluminum having an oxide coating on the surface
thereof, said aluminum is first made active by removing said
oxide coating.

100. A silver-plated copper-seeded aluminum powder
according to claim 96 wherein said noble metal is silver;
said non-noble metal substrate material is aluminum powder
having spherical particles with a mean diameter of from 5 to
15 microns, which has been seeded with copper atoms; the
weight of silver plating coated onto said copper-seeded
aluminum powder is from 15 to 60 weight percent, based on the
total weight of final silver-plated copper-seeded aluminum
powder product; said starter plating solution is divided into
2 equal portions with 2 said individual plating solution
baths being prepared therefrom, such that 50% of the total
amount of free ions of noble metal to be plated out is
contained in each individual plating solution bath; the first
individual plating solution bath is maintained at a
temperature of from about 25 °C to about 35 °C; the second
individual plating solution bath is maintained at a
temperature of from about 60 °C to about 70 °C; said first
series of water rinses is performed once and comprises
rinsing twice in succession with cold water; said second
series of rinses is repeated 4 times in succession after
completion of said first series of rinses following plating
in the second individual plating solution bath, and comprises
the sequence of rinsing once with hot water; rinsing once
with a 25% glacial acetic acid aqueous solution; rinsing a
second time with hot water; and rinsing once with methanol;
said third series of rinses is performed once and comprises
the sequence of rinsing 3 times with hot water, followed by
rinsing 3 times with methanol; and said process further
comprises initially performing, before said first plating, a
cleaning and activating of said aluminum powder; seeding said
aluminum powder with copper atoms; and mixing the copper-seeded
aluminum powder with liquid detergent.

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101. The silver-plated copper-seeded aluminum powder
according to claim 100 wherein the weight of silver plating
coated onto said copper-seeded aluminum powder is from 15.0
to 25.0 weight percent, based on the total weight of final
silver-plated copper-seeded aluminum powder product.

102. The silver-plated copper-seeded aluminum powder
according to claim 100 wherein the weight of silver plating
coated onto said copper-seeded aluminum powder is 20.3 weight
percent, based on the total weight of final silver-plated
copper-seeded aluminum powder product; said first individual
plating solution bath is maintained at a temperature of about
32 °C; and said second individual plating solution bath is
maintained at a temperature of about 65 °C.

103. A gold-plated copper-seeded aluminum powder
according to claim 96 wherein said noble metal is gold; said
non-noble metal substrate material is aluminum powder having
spherical particles with a mean diameter of from 5 to 15
microns, which has been seeded with copper atoms; the weight
of gold plating coated onto said copper-seeded aluminum
powder is from 15 to 60 weight percent, based on the total
weight of final gold-plated copper-seeded aluminum powder
product; said starter plating solution is divided into 2
equal portions with 2 said individual plating solution baths
being prepared therefrom, such that 50% of the total amount
of free ions of noble metal to be plated out is contained in
each individual plating solution bath; the first individual
plating solution bath is maintained at a temperature of from
about 25 °C to about 35 °C; the second individual plating
solution bath is maintained at a temperature of from about 60
°C to about 70 °C; said first series of water rinses is
performed once and comprises rinsing twice in succession with
cold water; said second series of rinses is repeated 4 times
in succession after completion of said first series of rinses
following plating in the second individual plating solution
bath, and comprises the sequence of rinsing once with hot
water; rinsing once with a 25% glacial acetic acid aqueous
solution; rinsing a second time with hot water; and rinsing



-102-
once with methanol; said third series of rinses is performed
once and comprises the sequence of rinsing 3 times with hot
water, followed by rinsing 3 times with methanol; and said
process further comprises initially performing, before said
first plating, a cleaning and activating of said aluminum
powder; seeding said aluminum powder with copper atoms; and
mixing the copper-seeded aluminum powder with liquid
detergent.

104. The gold-plated copper-seeded aluminum powder
according to claim 103 wherein the weight of gold plating
coated onto said copper-seeded aluminum powder is from 15.0
to 25.0 weight percent, based on the total weight of final
gold-plated copper-seeded aluminum powder product.

105. A platinum-plated copper-seeded aluminum powder
according to claim 96 wherein said noble metal is platinum;
said non-noble metal substrate material is aluminum powder
having spherical particles with a mean diameter of from 5 to
15 microns, which has been seeded with copper atoms; the
weight of platinum plating coated onto said copper-seeded
aluminum powder is from 15 to 60 weight percent, based on the
total weight of final platinum-plated copper-seeded aluminum
powder product; said starter plating solution is divided into
2 equal portions with 2 said individual plating solution
baths being prepared therefrom, such that 50% of the total
amount of free ions of noble metal to be plated out is
contained in each individual plating solution bath; the first
individual plating solution bath is maintained at a
temperature of from about 25 °C to about 35 °C; the second
individual plating solution bath is maintained at a
temperature of from about 60 °C to about 70 °C; said first
series of water rinses is performed once and comprises
rinsing twice in succession with cold water; said second
series of rinses is repeated 4 times in succession after
completion of said first series of rinses following plating
in the second individual plating solution bath, and comprises
the sequence of rinsing once with hot water; rinsing once
with a 25% glacial acetic acid aqueous solution; rinsing a

-103-

second time with hot water; and rinsing once with methanol;
said third series of rinses is performed once and comprises
the sequence of rinsing 3 times with hot water, followed by
rinsing 3 times with methanol; and said process further
comprises initially performing, before said first plating, a
cleaning and activating of said aluminum powder; seeding said
aluminum powder with copper atoms; and mixing the copper-seeded
aluminum powder with liquid detergent.

106. The platinum-plated copper-seeded aluminum powder
according to claim 105 wherein the weight of platinum plating
coated onto said copper-seeded aluminum powder is from 15.0
to 25.0 weight percent, based on the total weight of final
platinum-plated copper-seeded aluminum powder product.

107. An electrically conductive composition comprising
a noble metal-coated, copper-seeded aluminum powder, with
aluminum particles having a mean diameter of from about 5
microns to about 15 microns, and an outer surface area, with
said aluminum powder containing copper in an amount of from
about 0.001 percent by weight to about 0.01 percent by
weight, based on the weight of aluminum powder, with said
copper-seeded aluminum powder being coated with a noble metal
selected from the group consisting of silver, gold, and
platinum, said noble metal being in an amount of from about
2 percent by weight to about 60 percent by weight, based on
the total weight of the composition; such that said noble
metal in said composition is present in an amount sufficient
to at least completely coat said outer surface area of said
copper-seeded aluminum powder, leaving no exposed surface
area of said copper-seeded aluminum powder uncoated with said
noble metal.

108. The composition according to claim 88 wherein said
non-noble metal substrate material containing a first
non-noble metal seeded with atoms of a second non-noble metal is
a solid solution of said first non-noble metal and said
second non-noble metal, such that said solid solution is
composed of a solid solute and a solid solvent, wherein said

-104-
first non-noble metal is said solvent of said solid solution
and said second non-noble metal is said solute of said solid
solution.

109. The composition according to claim 108 wherein said
solid solution of said first non-noble metal and said second
non-noble metal is a substitutional solid solution when atoms
of said second non-noble metal have a diameter which is
substantially the same size as the diameter of atoms of said
first non-noble metal; and wherein said solid solution of
said first non-noble metal and said second non-noble metal is
an interstitial solid solution when atoms of said second
non-noble metal have a diameter which is less than about 59% of
the diameter of atoms of said first non-noble metal.

110. The composition according to claim 88 wherein said
second non-noble metal constitutes from about 0.001 to about
0.01 weight percent of said non-noble metal substrate
material.

111. The composition according to claim 96 wherein in
(e) the temperature of said individual plating solution bath
is inversely related to the oxidation potential of the
non-noble metal substrate material being plated;
with the temperature of a first individual plating
solution bath being at up to about 32 °C when said first
non-noble metal of said non-noble metal substrate material is
aluminum;
with the temperature of a first individual plating
solution bath being at up to about 70 °C when said first
non-noble metal of said non-noble metal substrate material is
copper; and
with the temperature of a first individual plating
solution bath being at up to about 80 °C when said first
non-noble metal of said non-noble metal substrate material is
nickel.


-105-
112. The process according to claim 96 wherein in (e)
the temperatures of said individual plating solution baths
are inversely related to the oxidation potential of the
non-noble metal substrate material being plated, with a lower
temperature within said range being selected when said
non-noble metal substrate material has a high oxidation
potential, and a higher temperature within said range being
selected when said non-noble metal substrate material has a
low oxidation potential.

113. The composition according to claim 96 wherein in
(e) the temperature of a first individual plating solution
bath is:
at up to about 32 °C when said first non-noble metal of
said non-noble metal substrate material is aluminum;
at up to about 70 °C when said first non-noble metal of
said non-noble metal substrate material is copper; and
at up to about 80 °C when said first non-noble metal of
said non-noble metal substrate material is nickel.

114. The composition according to claim 96 wherein in
(a) the seeding of said first non-noble metal of said
substrate material with atoms of said second non-noble metal
of said substrate material is performed by washing said first
non-noble metal with a liquid solution containing atoms of
said second non-noble metal, such that substantially all of
said atoms of said second non-noble metal come out of said
liquid solution leaving a lean solution, followed by
decanting of said lean solution, to produce a dual non-noble
metal substrate in which said atoms of said second non-noble
metal are seeded among said first non-noble metal.

115. The composition according to claim 96 wherein said
non-noble metal substrate material containing a first
non-noble metal seeded with atoms of a second non-noble metal is
a solid solution of said first non-noble metal and said
second non-noble metal, such that said solid solution is
composed of a solid solute and a solid solvent, wherein said
first non-noble metal is said solvent of said solid solution


-106-
and said second non-noble metal is said solute of said solid
solution.

116. The composition according to claim 115 wherein said
solid solution of said first non-noble metal and said second
non-noble metal is a substitutional solid solution when atoms
of said second non-noble metal have a diameter which is
substantially the same size as the diameter of atoms of said
first non-noble metal; and wherein said solid solution of
said first non-noble metal and said second non-noble metal is
an interstitial solid solution when atoms of said second
non-noble metal have a diameter which is less than about 59% of
the diameter of atoms of said first non-noble metal.

117. The composition according to claim 96 wherein said
second non-noble metal constitutes from about 0.001 to about
0.01 weight percent of said non-noble metal substrate
material.

118. The silver-plated copper-seeded aluminum powder
according to claim 100 wherein said copper constitutes from
about 0.001 to about 0.01 weight percent of said copper-seeded
aluminum powder.

119. The gold-plated copper-seeded aluminum powder
according to claim 103 wherein said copper constitutes from
about 0.001 to about 0.01 weight percent of said copper-seeded
aluminum powder.

120. The platinum-plated copper-seeded aluminum powder
according to claim 105 wherein said copper constitutes from
about 0.001 to about 0.01 weight percent of said copper-seeded
aluminum powder.

121. A noble metal plated non-noble substrate produced
according to the process of claim 1.

122. A silver plated copper powder produced according to
the process of claim 42.

-107-

123. A silver plated copper powder produced according to
the process of claim 45.

124. A silver plated nickel powder produced according to
the process of claim 46.

125. A silver plated nickel powder produced according to
the process of claim 50.

126. A silver plated copper-seeded aluminum powder
produced according to the process of claim 51.

127. A silver plated copper-seeded aluminum powder
produced according to the process of claim 62.

128. A gold plated nickel powder produced according to
the process of claim 63.

129. A gold plated nickel powder produced according to
the process of claim 67.

130. A coated metal powder comprising aluminum powder
seeded with an effective amount of a different non-noble
seeding metal having a greater affinity for a noble metal
with which the seeded aluminum powder is coated than for said
aluminum powder, such that the seeded aluminum powder is
completely covered with the noble metal.

131. The coated metal powder according to claim 130
wherein the aluminum powder has spherical-shaped particles
with a mean diameter of from 5 to 15 microns.

132. The coated metal powder according to claim 130
wherein the noble metal is selected from the group consisting
of silver, gold and platinum.

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133. The coated metal powder according to claim 130
wherein the noble metal coating the seeded aluminum powder is
in an amount of from 2 to 60 weight percent, based on the
final total weight of the coated powder.

134. The coated metal powder according to claim 130
wherein the seeding metal is present in an amount of at least
0.001 weight percent, based on the weight of aluminum.

135. The coated metal powder according to claim 130
wherein the seeding metal is copper.

136. The coated metal powder according to claim 130
wherein the seeding metal is copper, in an amount of about
0.05 weight percent, based on the weight of aluminum, and the
noble metal is silver, in an amount of from about 15 to about
25 weight percent, based on the final total weight of the
coated powder.

137. Silver-coated, copper-seeded aluminum powder.

138. An electromagnetic interference shielding material
comprising:
a matrix material filled with a noble metal plated
non-noble metal substrate,
wherein the noble metal plated non-noble metal substrate
is produced by the electroless deposition of the noble metal,
selected from the group consisting of silver, gold, platinum,
palladium, irridium, rhodium, ruthenium and osmium, onto the
substrate, selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, thalium and combinations of a principal one of the
foregoing substrate materials seeded with atoms of another
one of the foregoing substrate materials having a greater
affinity than the principal substrate material for the noble
metal being plated thereon,
from a plurality of aqueous solution plating baths
prepared by division into said plurality of baths of a


-109-

starter aqueous plating solution containing a total quantity
of free noble metal ions sufficient to plate the non-noble
metal substrate with a selected amount of noble metal coating
of from 2-60 percent of the total weight of final coated
substrate, such that each of said plurality of baths contains
a specified fraction of the total amount of free noble metal
ions to be deposited, and is brought to a specified
concentration by the addition of water thereto;
and further wherein the free noble metal ions are
deposited onto the substrate from a first one of the plating
solution baths maintained at a temperature in the range of
from about 20 °C to about 100 °C, until the plating solution
bath is substantially depleted of free noble metal ions,
thereby forming a first intermediate plated substrate which
is separated from the depleted plating solution bath, rinsed
at least once with a first series of rinse steps selected
from the group consisting of rinsing twice in succession with
cold water; rinsing once with warm water, followed by rinsing
once with hot water; and rinsing twice in succession with hot
water;
the final plated substrate, coated with the total amount
of noble metal ions in the original starter plating solution,
is prepared by repeating the deposition, separation and first
rinsing sequence steps with the intermediate plated substrate
from the previous sequence of steps to form a next plated
substrate, cumulatively plated with the fractions of noble
metal ions contained in the subsequent plating solution baths
into which the substrate has been immersed, until all of said
plating solution baths have been utilized;
the final plated substrate then being rinsed at least
once with a second series of rinse steps, including rinsing
once with hot water, rinsing once with a weak acid selected
from the group consisting of aqueous solutions of glacial
acetic acid, dilute hydrochloric acid, dilute nitric acid,
and hydrazine; rinsing a second time with hot water, and
rinsing once with an alcohol selected from the group
consisting of lower alkanols having from 1 to 4 carbon atoms;
rinsing at least once with a third series of rinse steps
including rinsing from 1 to 3 times in succession with hot

-110-
water, followed by rinsing from 1 to 3 times in succession
with an alcohol selected from the group consisting of lower
alkanols having from 1 to 4 carbon atoms; and
drying to form the final noble metal plated non-noble
metal substrate for use in the shielding material.

139. The electromagnetic interference shielding material
of claim 138 wherein the matrix material is selected from the
group consisting of a rubber, a plastic material, an elastic
material and mixtures thereof.

140. The electromagnetic interference shielding material
of claim 139 wherein the elastic material is a silicone, a
fluorosilicone or a polyisobutylene elastomer; and the
plastic material is a polyamide, an acrylic, a urethane, or
a polyvinyl chloride silicone plastic.

141. The electromagnetic interference shielding material
according to claim 140 wherein the noble metal plated
non-noble metal substrate is a silver plated copper powder.

142. The electromagnetic interference shielding material
according to claim 140 wherein the noble metal plated
non-noble metal substrate is a silver plated nickel powder.

143. An electromagnetic interference shielding material
comprising a matrix material selected from the group
consisting of a rubber, a plastic material, an elastic
material and mixtures thereof, which is filled with an amount
of a silver plated, copper-seeded aluminum powder.

144. The electromagnetic interference shielding material
according to claim 140 wherein the noble metal plated
non-noble metal substrate is a silver plated, copper-seeded
aluminum powder.


-111-
145. An electromagnetic interference shielding material
comprising a matrix material selected from the group
consisting of a rubber, a plastic material, an elastic
material and mixtures thereof, which is filled with an amount
of a gold or silver plated nickel powder.

146. The electromagnetic interference shielding material
according to claim 140 wherein the noble metal plated
non-noble metal substrate is a gold plated nickel powder.

147. The electromagnetic interference shielding material
according to claim 141 wherein the copper powder has
spherical shaped particles with a mean diameter of from 5 to
15 microns; the weight of coating is from 15 to 60 weight
percent of the total weight of final coated powder; the
starter plating solution is divided into 5 portions with the
plating solution baths prepared therefrom containing,
respectively, from 75% to 85% of the total noble metal ions
to be plated in the first bath; 10% to 20% of the total
noble metal ions to be plated in the second bath; 1% to
5% of the total noble metal ions to be plated in the third
bath; and 0.1% to 0.5% of the total noble metal ions to be
plated in each of the fourth and fifth baths, such that the
total of all fractions in the 5 baths is 1.0; the first bath
is maintained at a temperature of from about 50 °C to about
80 °C; the second through fifth baths are maintained at a
temperature of from about 85 °C to about 100 °C; the first
series of rinse steps is performed once and comprises the
sequence of steps of rinsing once with warm water followed by
rinsing once with hot water; the second series of rinse steps
is repeated 4 times in succession after completion of the
first series of rinses following plating in the fifth plating
solution bath and comprises the sequence of steps of rinsing
once with hot water; rinsing once with 25% glacial acetic
acid aqueous solution; rinsing a second time with hot water;
and rinsing once with methanol; and the third series of
rinses is performed once and comprises the sequence of steps
of rinsing 3 times with hot water, followed by rinsing 3
times with methanol; and further comprising performing a

-112-

second series of rinse steps once after completion of the
first series of rinse steps which follows after plating in
the third plating solution bath.

148. The electromagnetic interference shielding material
according to claim 147 wherein the weight of coating is 17.6
weight percent of the total weight of final coated powder and
the plating solution baths contain, respectively, 80% of the
total noble metal ions to be plated in the first bath; 16%
of the total noble metal ions to be plated in the 25 second
bath; 3-2% of the total noble metal ions to be plated in the
third bath; and 0-4% of the total noble metal ions to be
plated in each of the fourth and fifth baths.

149. The electromagnetic interference shielding material
according to claim 142 wherein the nickel powder has
spherical shaped particles with a mean diameter of from 5 to
15 microns; the weight of coating is from 15 to 60 weight
percent of the total weight of coated powder; the starter
plating solution is divided into 4 equal portions with the
plating solution baths prepared therefrom each containing
0.25 of the total noble metal ions to be plated; the first
bath is maintained at a temperature of from about 50 °C to
about 80 °C; the second through fourth baths are maintained
at a temperature of from about 85 °C to about 100 °C; the
first series of rinse steps comprises the sequence steps of
rinsing twice with hot water; the second series of rinse
steps is repeated 4 times in succession after completion of
the first series of rinses following plating in the fourth
plating solution bath and comprises the sequence of steps of
rinsing once with hot water; rinsing once with 25% glacial
acetic acid aqueous solution; rinsing a second time with hot
water; and rinsing once with methanol; and the third series
of rinses is performed once and comprises the sequence of
steps of rinsing 3 times with hot water, followed by rinsing
3 times with methanol; and further comprising cleaning and
activating the nickel powder substrate prior to its immersion
in the first plating solution bath.

-113-

150. The electromagnetic interference shielding material
according to claim 149 wherein the weight of coating is 16.0
weight percent of the total weight of final coated powder,
the first bath is maintained at a temperature of about 75 °C;
and the second through fourth baths are maintained at a
temperature of about 100 °C.

151. The electromagnetic interference shielding material
according to claim 144 wherein the aluminum powder seeded
with copper atoms has spherical shaped particles with a mean
diameter of from 5 to 15 microns and seeded with copper
atoms; the weight of coating is from 15 to 60 weight percent
of the total weight of final coated powder; the starter
plating solution is divided into 2 equal portions with the
plating solution baths prepared there- from each containing
50% of the total noble metal ions to be plated; the first
bath is maintained at a temperature of from about 25 °C to
about 35 °C; the second bath is maintained at a temperature
of from about 60 °C to about 70 °C; the first series of rinse
steps is performed once and comprises rinsing twice in
succession with cold water; the second series of rinse steps
is repeated 4 times in succession after completion of the
first series of rinses following plating in the second
plating solution bath and comprises the sequence of steps of
rinsing once with hot water; rinsing once with 25% glacial
acetic acid aqueous solution; rinsing a second time with hot
water; and rinsing once with methanol; and the third series
of rinses is performed once and comprises the sequence of
steps of rinsing 3 times with hot water, followed by rinsing
3 times with methanol; and still further comprising the
initial steps of cleaning and activating the aluminum powder;
seeding the aluminum powder with copper atoms; and mixing the
copper-seeded aluminum powder with liquid detergent before
the first plating step.

152. The electromagnetic interference shielding material
according to claim 151 wherein the weight of coating is 20.3
weight percent of the total weight of final coated powder,
the first bath is maintained at a temperature of about 32 °C;


-114-

and the second bath is maintained at a temperature of about
65 °C

153. The electromagnetic interference shielding material
according to claim 146 wherein the nickel powder has
spherical shaped particles with a mean diameter of from 8 to
10 microns; the weight of coating is from 15 to 60 weight
percent of the total weight of coated powder; the starter
plating solution is divided into 4 equal portions with the
plating solution baths prepared therefrom each containing
25% of the total noble metal ions to be plated; the first
bath is maintained at a temperature of from about 50 °C to
about 80 °C; the second through fourth baths are maintained
at a temperature of from about 85 °C to about 100 °C; the
first series of rinse steps comprises the sequence steps of
rinsing twice with hot water; the second series of rinse
steps is repeated 4 times in succession after completion of
the first series of rinses following plating in the fourth
plating solution bath and comprises the sequence of steps of
rinsing once with hot water; rinsing once with 25% glacial
acetic acid aqueous solution; rinsing a second time with hot
water; and rinsing once with methanol; and the third series
of rinses is performed once and comprises the sequence of
steps of rinsing 3 times with hot water, followed by rinsing
3 times with methanol; the process further comprising
cleaning and activating the nickel powder substrate prior to
its immersion in the first plating solution bath..

154. The electromagnetic interference shielding material
according to claim 153 wherein the weight of coating is 16.0
weight percent of the total weight of final coated powder,
the first bath is maintained at a temperature of about 75 °C;
and the second through fourth baths are maintained at a
temperature of from about 94 °C to about 98 °C.

155. An electrically conductive material comprising a
copolymer matrix containing at least one compound selected
from the group consisting of chlorinated biphenyl,
chlorinated triphenyl, amorphous polypropylene, ethylene,




-115-

vinyl acetate, phenol, formaldehyde, and terpine, together
with a noble metal coated non-noble metal substrate,
wherein the noble metal plated non-noble metal substrate
is produced by the electroless deposition of the noble metal,
selected from the group consisting of silver, gold, platinum,
palladium, irridium, rhodium, ruthenium and osmium, onto the
substrate, selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, thalium and combinations of a principal one of the
foregoing substrate materials seeded with atoms of another
one of the foregoing substrate materials having a greater
affinity than the principal substrate material for the noble
metal being plated thereon,
from a plurality of aqueous solution plating baths
prepared by division into said plurality of baths of a
starter aqueous plating solution containing a total quantity
of free noble metal ions sufficient to plate the non-noble
metal substrate with a selected amount of noble metal coating
of from 2-60 percent of the total weight of final coated
substrate, such that each of said plurality of baths contains
a specified fraction of the total amount of free noble metal
ions to be deposited, and is brought to a specified
concentration by the addition of water thereto;
and further wherein the free noble metal ions are
deposited onto the substrate from a first one of the plating
solution baths maintained at a temperature in the range of
from about 20 °C to about 100 °C, until the plating solution
bath is substantially depleted of free noble metal ions,
thereby forming a first intermediate plated substrate which
is separated from the depleted plating solution bath, rinsed
at least once with a first series of rinse steps selected
from the group consisting of rinsing twice in succession with
cold water; rinsing once with warm water, followed by rinsing
once with hot water; and rinsing twice in succession with hot
water;
the final plated substrate, coated with the total amount
of noble metal ions in the original starter plating solution,
is prepared by repeating the deposition, separation and first




-116-

rinsing sequence steps with the intermediate plated substrate
from the previous sequence of steps to form a next plated
substrate, cumulatively plated with the fractions of noble
metal ions contained in the subsequent plating solution baths
into which the substrate has been immersed, until all of said
plating solution baths have been utilized;
the final plated substrate then being rinsed at least
once with a second series of rinse steps, including rinsing
once with hot water, rinsing once with a weak acid selected
from the group consisting of aqueous solutions of glacial
acetic acid, dilute hydrochloric acid, dilute nitric acid,
and hydrazine; rinsing a second time with hot water, and
rinsing once with an alcohol selected from the group
consisting of lower alkanols having from 1 to 4 carbon atoms;
rinsing at least once with a third series of rinse steps
including rinsing from 1 to 3 times in succession with hot
water, followed by rinsing from 1 to 3 times in succession
with an alcohol selected from the group consisting of lower
alkanols having from 1 to 4 carbon atoms; and
drying to form the final noble metal plated non-noble
metal substrate for use in the electrically conductive
material.

156. An electrically conductive thermosetting plastic
comprising a modified polyamine, xylene solvent,
diisocyanate, and toluene solvent, together with a noble
metal coated non-noble metal substrate
wherein the noble metal plated non-noble metal substrate
is produced by the electroless deposition of the noble metal,
selected from the group consisting of silver, gold, platinum,
palladium, irridium, rhodium, ruthenium and osmium, onto the
substrate, selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, thalium and combinations of a principal one of the
foregoing substrate materials seeded with atoms of another
one of the foregoing substrate materials having a greater
affinity than the principal substrate material for the noble
metal being plated thereon,


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from a plurality of aqueous solution plating baths
prepared by division into said plurality of baths of a 25
starter aqueous plating solution containing a total quantity
of free noble metal ions sufficient to plate the non-noble
metal substrate with a selected amount of noble metal coating
of from 2-60 percent of the total weight of final coated
substrate,
and further wherein the free noble metal ions are
deposited onto the substrate from a first one of the plating
solution baths maintained at a temperature in the range of
from about 20 °C to about 100 °C, until the plating solution
bath is substantially depleted of free noble metal ions,
thereby forming a first intermediate plated substrate which
is separated from the depleted plating solution bath, rinsed
at least once with a first series of rinse steps selected
from the group consisting of rinsing twice in succession with
cold water; rinsing once with warm water, followed by rinsing
once with hot water; and rinsing twice in succession with hot
water;
the final plated substrate, coated with the total amount
of noble metal ions in the original starter plating solution,
is prepared by repeating the deposition, separation and first
rinsing sequence steps with the intermediate plated substrate
from the previous sequence of steps to form a next plated
substrate, cumulatively plated with the fractions of noble
metal ions contained in the subsequent plating solution baths
into which the substrate has been immersed, until all of said
plating solution baths have been utilized;
the final plated substrate then being rinsed at least
once with a second series of rinse steps, including rinsing
once with hot water, rinsing once with a weak acid selected
from the group consisting of aqueous solutions of glacial
acetic acid, dilute hydrochloric acid, dilute nitric acid,
and hydrazine; rinsing a second time with hot water, and
rinsing once with an alcohol selected from the group
consisting of lower alkanols having from 1 to 4 carbon atoms;
rinsing at least once with a third series of rinse steps
including rinsing from 1 to 3 times in succession with hot 10
water, followed by rinsing from 1 to 3 times in succession



- 118-


with an alcohol selected from the group consisting of lower
alkanols having from 1 to 4 carbon atoms; and
drying to form the final noble metal plated non-noble
metal substrate for use in the electrically conductive
thermosetting plastic.

157. An electrically conductive adhesive material
comprising chlorinated biphenyl, chlorinated triphenyl, and
amorphous polypropylene, together with a noble metal coated
non-noble metal substrate
wherein the noble metal plated non-noble metal substrate
is produced by the electroless deposition of the noble metal,
selected from the group consisting of silver, gold, platinum,
palladium, irridium, rhodium, ruthenium and osmium, onto the
substrate, selected from the group consisting of copper,
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, thalium and combinations of a principal one of the
foregoing substrate materials seeded with atoms of another
one of the foregoing substrate materials having a greater
affinity than the principal substrate material for the noble
metal being plated thereon,
from a plurality of aqueous solution plating baths
prepared by division into said plurality of baths of a
starter aqueous plating solution containing a total quantity
of free noble metal ions sufficient to plate the non-noble
metal substrate with a selected amount of noble metal coating
of from 2-60 percent of the total weight of final coated
substrate, such that each of said plurality of baths contains
a specified fraction of the total amount of free noble metal
ions to be deposited, and is brought to a specified
concentration by the addition of water thereto;
and further wherein the free noble metal ions are
deposited onto the substrate from a first one of the plating
solution baths maintained at a temperature in the range of
from about 20 °C to about 100 °C, until the plating solution
bath is substantially depleted of free noble metal ions,
thereby forming a first intermediate plated substrate which
is separated from the depleted plating solution bath, rinsed

-119-
at least once with a first series of rinse steps selected
from the group consisting of rinsing twice in succession with
cold water; rinsing once with warm water, followed by rinsing
once with hot water; and rinsing twice in succession with hot
water;
the final plated substrate, coated with the total amount
of noble metal ions in the original starter plating solution,
is prepared by repeating the deposition, separation and first
rinsing sequence steps with the intermediate plated substrate
from the previous sequence of steps to form a next plated
substrate, cumulatively plated with the fractions of noble
metal ions contained in the subsequent plating solution baths
into which the substrate has been immersed, until all of said
plating solution baths have been utilized;
the final plated substrate then being rinsed at least
once with a second series of rinse steps, including rinsing
once with hot water, rinsing once with a weak acid selected
from the group consisting of aqueous solutions of glacial
acetic acid, dilute hydrochloric acid, dilute nitric acid,
and hydrazine; rinsing a second time with hot water, and
rinsing once with an alcohol selected from the group
consisting of lower alkanols having from 1 to 4 carbon atoms;
rinsing at least once with a third series of rinse steps
including rinsing from 1 to 3 times in succession with hot
water, followed by rinsing from 1 to 3 times in succession
with an alcohol selected from the group consisting of lower
alkanols having from 1 to 4 carbon atoms; and
drying to form the final noble metal plated non-noble
metal substrate for use in the electrically conductive
adhesive material.

158. An electrically conductive material comprising a
polyamide resin and an epoxy, together with a noble metal
coated non-noble metal substrate
wherein the noble metal plated non-noble metal substrate
is produced by the electroless deposition of the noble metal,
selected from the group consisting of silver, gold, platinum,
palladium, irridium, rhodium, ruthenium and osmium, onto the
substrate, selected from the group consisting of copper,


-120-
nickel, aluminum, titanium, zirconium, vanadium, hafnium,
cadmium, niobium, tantalum, molybdenum, tungsten, gallium,
indium, thalium and combinations of a principal one of the
foregoing substrate materials seeded with atoms of another
one of the foregoing substrate materials having a greater
affinity than the principal substrate material for the noble
metal being plated thereon,
from a plurality of aqueous solution plating baths
prepared by division into said plurality of baths of a
starter aqueous plating solution containing a total quantity
of free noble metal ions sufficient to plate the non-noble
metal substrate with a selected amount of noble metal coating
of from 2-60 percent of the total weight of final coated
substrate, such that each of said plurality of baths contains
a specified fraction of the total amount of free noble metal
ions to be deposited, and is brought to a specified
concentration by the addition of water thereto;
and further wherein the free noble metal ions are
deposited onto the substrate from a first one of the plating
solution baths maintained at a temperature in the range of
from about 20 °C to about 100 °C, until the plating solution
bath is substantially depleted of free noble metal ions,
thereby forming a first intermediate plated substrate which
is separated from the depleted plating solution bath, rinsed
at least once with a first series of rinse steps selected
from the group consisting of rinsing twice in succession with
cold water; rinsing once with warm water, followed by rinsing
once with hot water; and rinsing twice in succession with hot
water;
the final plated substrate, coated with the total amount
of noble metal ions in the original starter plating solution,
is prepared by repeating the deposition, separation and first
rinsing sequence steps with the intermediate plated substrate
from the previous sequence of steps to form a next plated
substrate, cumulatively plated with the fractions of noble
metal ions contained in the subsequent plating solution baths
into which the substrate has been immersed, until all of said
plating solution baths have been utilized;

-121-

the final plated substrate then being rinsed at least
once with a second series of rinse steps, including rinsing
once with hot water, rinsing once with a weak acid selected
from the group consisting of aqueous solutions of glacial 25
acetic acid, dilute hydrochloric acid, dilute nitric acid,
and hydrazine; rinsing a second time with hot water, and
rinsing once with an alcohol selected from the group
consisting of lower alkanols having from 1 to 4 carbon atoms;
rinsing at least once with a third series of rinse steps
including rinsing from 1 to 3 times in succession with hot
water, followed by rinsing from 1 to 3 times in succession
with an alcohol selected from the group consisting of lower
alkanols having from 1 to 4 carbon atoms; and
drying to form the final noble metal plated non-noble
metal substrate for use in the electrically conductive lo
material.

159. The electromagnetic interference shielding material
according to claim 142 wherein the matrix is from about 5 to
about 20 weight percent of the overall material, and the
noble metal coated non-noble metal powder is from about 95 to
about 80 weight percent of the overall material.


Description

Note: Descriptions are shown in the official language in which they were submitted.


~ ~39~



FIELD OF THE INVENTION



This invention relates to a process for producing a
coating of a noble metal onto a non-noble metal substrate.
More particularly, the invention relates to a process for
preparing electrically conductive non-noble metallic
particles with a noble metal coating. Still more
particularly, the invention relates to a process for
preparing an electrically conductive powder in the form of a
non-noble metal such as copper, nickel, aluminum and the
like, coated with a noble metal such as silver, gold,
platinum and the like. The invention especially relates to
the preparation of an electrically conductive silver-coated
copper powder, an electrically conductive silver-coated
nickel powder, an electrically conductive silver-coated
aluminum powder, and an electrically conductive gold-coated
nickel powder. The invention also relates to the preparation
of useful products incorporating the above coated materials,
including electromagnetic interference shielding materials
in which the coated materials are incorporated in a rubber
matrix, electrically conductive adhesives, and electrically
conductive inks.




BACRGROUND OF THE INVENTION



Electrically conductive noble metal-coated metallic
particles, especially powders, are an important additive in

~3~sla


the preparation of electrically conductive plastics,
adhesives and inks, and in resin matrix based
electromagnetic interference shielding materials.
The most commercially useful of such coated particles
and powders are those wherein copper, nickel or aluminum
substrates are coated with silver or gold. A number of
processes have been developed over the years for the
preparation of such noble metal-coated metallic materials.
For example, U.S. Patent 3,202,488 to Ehrreich et al for

"Silver-Plated Copper Powder" discloses a process for
preparing silver-plated copper powder by replacement plating
silver from silver cyanide solution whereby copper ions on
the surface of the copper powder are replaced with silver
ions from the solution.

U.S. Patent 2,771,380 to Coleman et al for "Method of
Plating Copper Particles ~ith Silver" discloses a process
for silver-plating copper particles requiring that the
copper particles first be dry-mixed with an agent which
maintains the copper particles in a separated or dispersed

condition, prior to immersion in an aqueous silver plating
bath.
U.S. Patent 4,450,188 to Rawasumi for "Process for the
Preparation of Precious Metal Coated Particles" discloses
processes for coating a metal core material with a precious
2; metal wherein a suspension of precious metal salt particles
and dissolved precious metal salt ions; or a solution of
dissolved precious metal salt ions; or a mixture of precious

metal ions and a chelate of a precious metal compound in a


~33q810



suspended phase, are alternatively mixed with an aqueous
suspension of core material particles, to carry out the
coating of the core with the precious metal in a gelling
suspension.
U.S. Patent 4,652,465 to Koto et al. for "Process for
the Production of a Silver Coated Copper Powder and
Conductive Coating Composition" discloses a process wherein
silver is precipitated on the surface of a copper powder by
means of a silver complex solution containing a silver salt,
an ammonium carbonate compound and ammonia water, which is
added dropwise to a suspension of copper powder,
alternatively, in water, in ammonia water, and in an aqueous
solution of an ammonium carbonate compound.
U.S. Patent 4,716,081 to Ehrreich for "Conductive
Compositions and Conductive Powders for Use Therein"
discloses a process for producing silver-coated non-noble
metal powders, principally copper, by replacement plating
from a solution containing ions of the noble metal,
essentially as disclosed in U.S. Patent 3,202,488, but
further requiring high temperature heat treatment of the
coated material at a temperature of 200 ~ C for from 24 to
several hundred hours or 150 ~ C from 70 to 1500 hours.
U.S. Patent 4,434,541 to Powers, Jr. for
"Electromagnetic Shielding" discloses a process for
preparing electromagnetic interference shielding materials
utilizing electrically conductive solid metal particles
consisting of an aluminum core on which it is first required
to coat a layer of tin, zinc or nickel prior to plating with


1339810


an outer coating of silver.
U.S. Patent 3,989,606 to Kampert for "Metal Plating On
Aluminum" discloses a process in which an aluminum substrate
is first immersion coated with zinc prior to being electro-

plated with nickel.
All of the above processes, however, have certaindisadvantages, which may result in the coated products
produced not being of uniformly and consistently high
quality, or the processes require some step, such as a long
duration high temperature heat treatment in order to produce
acceptable product, but which renders the process
impractical and uneconomical for large scale commercial use.
Some of the above processes have the disadvantage of
requiring that the substrate material first be plated with
15 an intermediate metal prior to coating with the precious
metal. One utilizes a combination of immersion coating to
produce the intermediate layer, followed by electro-plating
to remove the intermediate layer and replace it with the
outer coating of precious metal. Such a dual process has the
20 disadvantage of also requiring a source of electricity, and
depending on the costs of electricity, can be prohibitively
costly in terms of both capital equipment costs and
operating costs. Regardless of whether the precious metal
coating is deposited by an immersion coating or an
25 electro-plating process, in either case, the outer coating
of precious metal may not completely coat or replace the
intermediate layer, particularly because the coating with
precious metal is performed in a single step, and may not be


133q81 ~



of uniform thickness, thereby affecting the physical and
electrical properties of the final coated product, such as
its corrosion resistance and electrical conductivity. In the
past, it has sometimes occurred that producers of the coated
5 materials have had to recoat the product after rejecting it
for not having passed their own in-house quality control
tests, or more embarrassingly, after rejection by their
customers as being off specification and unacceptable for
the intended end use. Both situations are costly to the
10 producer, either in an economic sense or from the
perspective of negatively affecting their business
reputation.
Other earlier processes have the disadvantage of
requiring the formation of suspensions or chelates of the
15 precious metal ions, or suspensions of the substrate
material, or both, and effect the coating reaction by a
complex and messy gel-forming reaction. Still others have
the disadvantage of requiring the addition of special
additives to the substrate or to the plating solution bath
20 in order to achieve a more acceptable quality of coated
product.
The single greatest disadvantage of all of the earlier
processes, however, has been the fact that they have been
based on a single coating step in which the total amount of
25 noble metal to be deposited is provided in one plating
solution bath. Such processes present difficulties with
respect to their capability of consistently producing
uniformly coated product of high quality.


~339:81~



When the entire coating is effected in a single step,
there is a tendency for uneven coating of all the substrate
particles to occur. Some particles of the non-noble metal
substrate can become coated with more than the desired
amount of noble metal, while other particles of the
substrate may be only partially coated or even completely
uncoated. The latter is especially true when the substrate
is a fine powder, having a large surface area.
Some of the parameters that play a major role in
affecting the extent of coating of the substrate particles
include the concentration of the noble metal ions in the
plating solution bath; the size of the substrate particles;
the homogeneity of the mixing and distribution of the
substrate particles in the plating solution bath; the
cleanliness and state of activation of the the substrate
material; and the efficiency of mixing and degree of contact
between substrate particles and noble metal ions in the
plating solution bath.
Where the substrate is a fine powder, local cohesive
forces between powder particles may be sufficiently strong
that they cannot be overcome when in the plating solution
bath, causing clumping of the substrate particles. These
clumps may remain even after stirring of the particles in
the bath. When such clumps form, the outer surface of the
particles to the center of a clump remains shielded against
plating by the noble metal ions. Some have attempted to
overcome this problem by introducing dispersing agents with
the substrate material, however, this alone does not


1 33981 0
--7--



completely overcome the problem, and, in fact, may create
other problems by introducing other chemical compounds into
the plating solution baths. Care must be taken that the
dispersing agent itself is chemically unreactive with
respect to the precious metal and that it does not interfere
with the coating process.
When coating is performed as a single step, there is
also a tendency for any impurities in the plating solution
bath to co-deposit on the surface of the substrate, together
lO with the noble metal ions. These impurities may then prevent
the subsequent plating of noble metal ions if the noble
metal ions have little affinity for the surface of the
impurities in comparison to the clean activated surface of
the substrate itself. In such cases, the surface of the
15 final product is an essentially noble metal coating
interspersed by impurities. Depending on the nature and
extent of the impurities, this phenomenon can greatly affect
the physical and electrical properties of the final coated
product. If the amount of impurities on the surface is large
20 and of a nature as to adversely affect the corrosion
resistance and electrical conductivity of the material, the
entire batch of coated product will be off specification and
unusable.
For example, the surface impurities may act as local
25 sites at which oxidation or corrosion of the material can
begin to occur. The impurities can also adversely change the
electrical conductivity of the coated material.
Alternatively, impurities in the plating solution bath

t339~10


may first deposit on the substrate surface and subsequently
become coated with noble metal, as long as the noble metal
ions in the plating solution bath have sufficient affinity
for coating the surface of the impurity. Where the bonding
5 or surface adhesive forces between the substrate and the
impurity or between the impurity and the noble metal which
subsequently coats it are not as great as exists between the
substrate and the the noble metal itself, however, the
coated product is susceptible to failure from several
10 possible causes. The noble metal coating may abrade from the
impurity leaving an exposed impurity or the noble
metal-bearing impurity may become abraded from the substrate
surface itself, leaving exposed substrate material.
Depending on the nature of the impurity or the substrate
15 material and the extent of the defect, either of these
situations can have a significant effect on the properties
of the coated product, possibly rendering it
off-specification and unusable.
Degradation of materials containing such defects after
20 incorporation in a finished product such as an
electromagnetic shielding material is also more likely and
can cause failure of the ultimate product. These defects can
have a significant negative effect on the electrical
conductivity of the material. Defects in the coated surface,
25 either as impurities or exposed substrate, can themselves
cause product failure by affecting the electrical properties
of the coated material, or they can act as localized sites
at which oxidation or corrosion may begin, ultimately


1 33981 0



leading to a change in the physical and electrical
properties of the material and failure of the product in
which the coated material has been incorporated. For
example, exposed copper substrate is highly susceptible to
5 corrosion if exposed to air or another oxygen-containing
atmosphere.
Accordingly, it is an object of the present invention to
teach a process that substantially eliminates all of the
aforesaid problems inherent in previous processes requiring
10 the formation of various suspensions or complexes, the
formation of intermediate metal coating layers, the addition
of special additives to promote the coating process, the use
of combined immersion and electroplating techniques, or,
generally, the use of only a single immersion coating step
15 to effect coating of the precious metal, and which assures
the consistent production of uniformly high quality coated
product through the use of a multi-step coating process,
with intermediate and final product rinsing steps.
The present invention is a significant improvement in
20 and major contribution to the state of the art of preparing
noble metal coated products in that it has been discovered
as a result of extensive experimentation and testing that
the aforesaid problems inherent in single plating step
processes are overcome and high quality coated product of
25 uniform consistency and long term stability is produced
utilizing a coating process comprising a plurality of
coating steps to plate-out the total desired amount of noble
metal onto the substrate, with each of the individual


1 33981 0

--10--

plating steps being followed by a series of washing steps
and a further series of washing steps being performed after
the last step of the washing sequence following the final
plating step.




SUMMARY OF THE INVENTION



In accordance with the invention, an improved process
for plating a coating of a noble metal onto a non-noble
metal substrate, especially for plating silver onto copper,
nickel and aluminum, is provided. A further object of the
10 invention is to provide such a coated material wherein the
particles of the substrate are coated in an economical,
efficient and rapid manner and the coated particles exhibit
high quality, highly uniform consistency and a high degree
of stability and reliability. Another object of the
15 invention is to provide a mass of noble metal coated
non-noble metal particles which exhibit electrical
properties substantially like solid particles of noble
metal, but which effect a considerable saving in the amount
of noble metal utilized. A still further object of the
20 invention is to provide a mass of noble metal coated
non-noble metal particles which can be produced as an

adhesive, dispersion, paint, conductor or wire for printed
circuits, a material for joining members by soldering or
welding, and a material which can be incorporated into a
25 plastic or resin matrix for use as an electromagnetic

1 33981 0

--11--

shielding material.
The process of the present invention comprises preparing
an aqueous plating solution containing free ions of the
noble metal; activating the non-noble metal substrate where
5 required by removing any metal oxide coating on the
substrate which prevents uniform coating; immersing the
activated substrate in a plurality of at least two baths of
the plating solution to coat the substrate with the metal
ions to a predetermined depth; washing the intermediately
10 coated and final coated substrate with water; next washing
the final coated substrate with at least one series of
rinses comprising a first rinse with water, a rinse with a
weak acid, a second rinse with water, and a rinse with an
alcohol; and finally rinsing the final coated substrate from
15 one to three times in succession with water and from one to
three times in succession with an alcohol.
The post-plating rinsing steps have been found to impart
to the final coated product consistently superior
characteristics than have heretofore been obtainable with
20 other immersion coating processes which do not include the
series of rinsing steps. These series of steps, in
combination with the use of a plurality of coating steps,
have been discovered to be responsible for the final coated
product having excellent electrical conductivity, uniformity
25 of coating and long term operational stability.

-12- 1339810

BRIEF DESCRIPTION OF THE DRAWINGS



Fig. l is a generalized block flow diagram of the
optional substrate material activation and pre-treatment
steps of the process of the invention.
Fig. 2 is a generalized block flow diagram of the master
plating solution preparation, plating, separation and first
rinse sequence steps of the process of the invention.
Fig. 3 is a generalized block flow diagram of the second
and third rinse sequence and drying steps of the process of
10 the invention.




DETAILED DESCRIPTION OF THE INVENTION



As used herein, the terms coating and plating, and their
respective derivative forms, are used interchangeably and
refer to the deposition of the noble metal on the non-noble
15 metal substrate by an electro-less process wherein the
substrate is immersed in a bath containing free ions of the
noble metal to produce a layer of the noble metal on the
non-noble metal substrate. Similarly, the terms noble metal
and precious metal are used interchangeably, and refer to
20 silver, gold, platinum and other valuable transition

elements of the periodic table. The terms rinse and wash are
used interchangeably in referring to the various inter- and
post-plating steps wherein the coated product is contacted
with various liquids as described in detail below.


1 33~8 1 0
-13-



The process of the present invention involves a
multi-step process of immersion coating a metallic powder in
a bath of noble metal-containing plating solution.
Noble metals which are platable according to this
5 process include gold, silver, platinum, palladium, iridium,
rhodium, ruthenium and osmium. Gold and silver are
particularly commercially significant.
Non-noble metal substrates onto which the noble metal is
plated according to this process include copper, nickel,
10 aluminum, titanium, zirconium, vanadium, hafnium, cadmium,
niobium, tantalum, molybdenum, tungsten, gallium, indium,
thallium and the like. Also included are combinations of one
of the above substrates seeded with atoms of another one of
the substrates having a greater affinity for the noble metal
15 plating material than the principal substrate material.
Copper, nickel, aluminum and copper-seeded aluminum are
especially preferred and of greatest commercial
significance. Titanium and zirconium are also of commercial
significance.
It has been found that the process works particularly
well for the plating of silver onto copper, silver or gold
onto nickel and silver onto copper-seeded aluminum.
The non-noble metal substrate onto which the noble metal
is plated is preferably in the form of a powder. The
particles of the powder can be in a variety of shapes,
including spheres, rods, or flakes. It has been found that
the best results are obtained when the particles of the
powder have a spherical shape. The plating of the noble


133981~



metal has been observed to be more uniform when spherically
shaped powders are used. In the case of plating silver onto
nickel powder, it is especially preferable that the powder
particles be spherical in shape.
The powders utilized as the substrates according to this
invention have a surface area of from 15 - 750 sq. ft/lb.
The particles of the powder should have a minimum size of
0.5 microns.
The first step of preparing the plating solution
involves a determination of how much noble metal is required
to produce the desired coating. Because it is difficult to
measure the thickness of the coating on micron sized powder
particles, it has long been the standard to measure the
amount of coating deposited on the substrate material as a
weight percent of the total weight of final coated product.
Accordingly, with the process of the invention it is
possible to produce coated products having from
approximately 2 to 60 weight percent noble metal coating on
the substrate material. Coatings amounting to less than
about 2 weight percent of the total weight of product tend
not to have completely and uniformly coated substrates,
particularly when the substrate particles being coated have
large volume and high surface area with respect to their
weight. Coatings greater than about 60 weight percent of the
25 total weight tend to be undesirable in that at such high
coating weights, the physical strength of the coated
particles begins to be negatively affected and the coating
material tends to easily abrade. Furthermore, higher coating


1 33981 0
-15-



weights of noble metal do not serve to enhance the
electrical properties of the coated material and are
wasteful of the more expensive noble metal.
The first step of the process of the present invention
involves the preparation of a master plating solution which
is substantially an aqueous solution containing the total
amount of free ions of the noble metal ultimately desired to
be coated onto the substrate.
There are a number of procedures for producing free
noble metal ion-containing aqueous solutions, that are known
to those skilled in the art. The following describes one
known method preferred for use in conjunction with the
process of the present invention. Other methods of effecting
dissolution of a noble metal-containing compound in aqueous
solution to generate a desired quantity of free noble metal
ions therein, for use as the master plating solution, may be
utilized and will be apparent to those skilled in the art.
Generally, the master plating solution is prepared by
dissolving in water a compound of the noble metal desired to
20 be coated onto the substrate, such as a cyanide, chloride,
or nitrate salt of the noble metal, or preferably, an oxide
of the noble metal. Because the cyanide, chloride and oxide
compounds of most noble metals range from being only
slightly soluble to insoluble in water, it is generally
25 necessary to add an amount of another compound to the
aqueous solution to act as an agent for promoting and
enhancing dissolution of the noble metal compound, so as to
generate the required amount of free noble metal ions in


13398tO
-16-



solution that will produce the amount of noble metal coating
on the substrate through the individual coating baths. The
cyanide, chloride and oxide forms of most noble metals are
soluble in cyanide-containing solutions. Therefore, an
alkali metal cyanide, which is itself readily soluble in
water, is used as the agent for promoting dissolution of the
noble metal compound in water. Potassium and sodium cyanide
are the preferred forms of alkali metal cyanide. The amount
of alkali metal cyanide used is from about 1.5 to 2.5 times
the weight of the noble metal compound providing the free
noble metal ions.
Preferably, the water for the master plating solution is
at or near the boiling point. The alkali metal cyanide is
slowly and carefully added to the boiling water before the
noble metal compound is introduced into the aqueous,
cyanide-containing solution, with constant stirring.
The nitrate compounds of most noble metals are generally
significantly more soluble in water than the cyanide,
chloride or oxide forms. Therefore, when a nitrate salt of a
20 noble metal is utilized as the source of the noble metal
ions for the master plating solution, little or no promoting
agent is required to generate the desired amount of free
noble metal ions in solution.
Where the noble metal to be coated onto the substrate is
25 gold, supplied as any form of gold compound, but
particularly as gold-potassium cyanide, it is known to those
skilled in the art to substitute for the use of an alkali
metal cyanide as a dissolution-promoting agent, the use of


-17- 1 33 98 1 0

an amount of at least one of ammonium chloride, sodium
citrate and sodium hypophosphate. Preferably, a mixture of
all three compounds in a weight ratio of ammonium chloride
to sodium citrate to sodium hypophosphate of from about 7.0
- 8.0 : 4.5 - 5.5 : 1 is used. When utilized as a mixture in
this ratio, the overall amount of mixture added to the water
of the master plating solution, prior to addition of the
gold-containing compound, is such that the weight of sodium
hypophosphate is from about 2.0 - 2.5 times the weight of
the gold-containing compound utilized.
For environmental reasons, it is generally preferred to
utilize the noble metal oxide form of the noble metal in
preparing the master plating solution to minimize the amount
of cyanide in the plating solution.
Where the non-noble metal substrate to be plated is one
which oxidizes, such as aluminum, the process includes a
step to remove the oxidation film so as to activate the
metal substrate whereby the noble metal belng plated onto
the substrate will adhere uniformly to the substrate. The
20 presence of an oxide coating on the substrate prevents good
adhesion of the plating metal.
Deoxidation of the surface of the substrate, where
required, is performed by any of a number of techniques
known in the art. It has been found that washing the
25 substrate with an aqueous solution of an alkali metal
cyanide is a particularly effective method of removing an
oxide coating from the surface of the substrate.
It has also been discovered that the plating process

~3398 1 0
-18-



itself is much improved by mixing a liquid detergent with
the particles of substrate material prior to immersing the
substrate in the plating solution baths. The liquid
detergent acts as a cleaning and brightening agent, and also
serves to moderate the speed of the plating reaction and
reduce or prevent foaming. It has been found that while the
use of a liquid detergent is not essential to the plating of
silver onto copper, it is very helpful in the plating of
silver onto a nickel substrate, and is essential for the
plating of silver onto aluminum.
In the case of plating a noble metal onto aluminum, it
has been discovered that plating is greatly facilitated and
the quality of the resulting product greatly improved when
the aluminum substrate material is first seeded with atoms
of another substrate material which is less oxidizable and
for which the plating metal ions have a greater affinity. It
is preferred to use copper as the seeding material for an
aluminum substrate material. The seeding material is readily
introduced into the substrate material by washing the
substrate with a solution containing ions of the seeding
material. Aluminum substrate material is effectively
coatable when the amount of seeding material is less than
0.01 weight percent of the substrate. The seeding material
can be as low as 0.001 weight percent of the substrate.
It has been found that in order to obtain the greatest
possible uniformity of coating, it is preferable that the
plating actually be carried out utilizing a plurality of
coating steps sequentially performed using a fresh plating

1339810
--19--

solution which is a fraction of a starter master plating
solution bath containing the total amount of noble metal to
be plated. Where a plurality of plating steps are utilized,
the total amount of noble metal ions to be deposited, as
calculated from consideration of the total weight of coating
to be applied is divided amongst the total number of plating
baths by taking the required fraction of the starter plating
solution and appropriately diluting each portion to give the
desired concentration.
It has been found that optimally from two to five plating
steps are generally sufficient to produce a uniform coating
of the noble metal on the substrate to whatever weight of
coating is desired. At least two steps, with intermediate
rinsing steps are required to produce a uniform coating and
to eliminate the problems of deposition of impurities that
occur with single plating step processes. It is not
necessary to have more than five plating steps with
intermediate rinsing steps. A diminishing return in terms of
increased process costs for insignificant improvement in the
quality of the coated product occurs beyond five plating
steps.
The optimum number of plating steps for a particular
plating situation is a function both of the nature of the
substrate material and the total amount of noble metal
coating being applied. The amount of noble metal to be
plated in any given plating step of a multi-step process
does not have to be the same, although it has been found
that for most substrate materials an equal division of the


1339810

-20-



total amount of noble metal among each of the plating
solution baths produces high quality product. Thus, it has
been discovered that the optimum number of plating solution
baths for plating silver or gold, particularly, a total
silver or gold content of from about 15 - 25 weight percent,
onto a nickel powder substrate is 4, with each bath
containing 25% by weight of the total amount of silver or
gold. Similarly, for the case of plating silver or gold,
particularly, a total silver or gold content of from about
15 - 25 weight percent, onto a copper-seeded aluminum
powder, it has been determined that 2 plating solution
baths, each containing 50% by weight of the total amount of
silver or gold produces optimum results. For plating silver
or gold, particularly a total silver or gold content of from
15 about 15 - 25 weight percent, onto copper powder, however,
it has been determined that 5 plating solution baths is the
optimum number required to produce a uniformly coated
product. For this case, however, it has been determined that
the optimum results are produced when the fraction of the
2~ total amount of silver or gold being plated is approximately
80 percent of the total amount by weight for the first
plating solution bath; approximately 16% for the second
bath; approximately 3.2% for the third bath; and
approximately 0.4% for each of the fourth and fifth baths.
According to the present invention, the plated substrate
is rinsed with a first series of rinse steps after
completion of each intermediate plating step as well as

after the final plating step. It has been found that these


1339810
-21-



washing steps, together with the feature of plating the
noble metal in a plurality of coating steps, greatly
improves the quality and consistency of the product. It is
believed that the rinse steps contribute to the high
5 quality, uniformity and stability of the coatings by acting
to remove trace amounts of impurities which have plated-out
on or have become adhered to the substrate material in the
preceding plating step, thereby preventing the accumulation
of impurities which would be coated-over in subsequent
plating steps, or as would immediately be coated-over in
single plating bath processes, a major factor responsible
for poor quality product and contributing to product failure
in service.
The intermediate and final first series of rinse steps
involve the simple washing of the intermediately or finally
coated substrate with water. It is preferred to use
distilled, demineralized and purified water to prevent the
introduction of new impurities in contact with the coated
substrate material. It has been found that two consecutive
20 water rinses are the optimum number of rinse steps in each
sequence for all cases of coating material and substrate. It
has been further found that the temperature of the water
rinses is, however, a factor affecting the efficiency of the
wash and the ability to remove impurities. The optimum
25 temperature moreover has been found to vary with the nature
of the coating material and substrate. Accordingly, it has
been found that for the case of plating silver onto a copper
substrate, optimum rinse efficiency is achieved by using


l 33q8l o


first a warm water rinse followed by a hot water rinse for
the second rinse of each two-rinse sequence. Similarly, for
the case of plating silver onto a nickel substrate, optimum
rinse efficiency is achieved using a hot water rinse for
each of the first and second rinse steps of each two-rinse
sequence. In the case of plating silver onto a copper-seeded
aluminum substrate it has been found that optimum rinse
efficiency is achieved using a cold water rinse for each of
the first and second rinse steps of each two-rinse sequence.
In addition to the post-intermediate plating step and
post-final plating step first sequence of rinse steps, it
has been found that performance of a second sequence of
rinse steps after completion of the last step of the
post-final plating step first rinse sequence further
15 improves the quality, consistency and stability of the final
coated product.
The second sequence of rinse steps is a four step series
of consecutive rinses; first, with water, preferably
distilled, demineralized and purified hot water; second,
20 with a weak aqueous acid solution, preferably a 25% by
volume glacial acetic acid aqueous solution; third, again
with water, as in the first step of the sequence; and
fourth, with an alcohol, preferably methanol. Other weak
acids which can be utilized in the second rinse step of the
25 sequence include dilute aqueous solutions of hydrochloric
acid, nitric acid and hydrazine. Other alcohols which can be
utilized in the fourth rinse step of the sequence include
all lower alkanols having from l to 4 carbon atoms.


1 33981 0

-23-



It has been found that the above series of rinses is an
optimum for the second sequence of rinse steps for all cases
of noble metals and substrate materials. Although it has
been found that optimum rinsing efficiency with the first
and third water rinse steps is achieved in all cases using
hot water, the second, acidic and fourth, alcohol rinse
steps can effectively be carried out using the respective
acid and alcohol solutions at essentially room temperature.
The complete sequence of four rinse steps should be
10 performed from one to four times in succession. It is
particularly preferred to repeat the second rinse step
sequence of four rinse steps the full four times.
It is believed that the second sequence of rinse steps
performed after the last water rinse step of the first
15 sequence following the last plating step contributes to the
overall quality, consistency and stability of the final
coated product by removing any remaining traces of
impurities which may have been introduced in the plating
solution baths or which may have originally been present on
20 the substrate material and which remained after any cleaning
and deoxidation of the substrate. The rinse steps also
appear to fix the plated noble metal by leaving a thin
coating which helps the coated product resist oxidation.
It has been found that the best final coated product is
25 obtained where yet one more sequence, that is, a third
sequence, of rinse steps is performed on the coated product
after completion of the last repetition of the four step

second sequence of rinse steps.


133981û
-24-



The third sequence of rinse steps includes a washing of
the coated product first from one to three times in
succession with hot water, followed by washing from one to
three times in succession with an alcohol. The alcohol can
be any lower alkanol having from l to 4 carbon atoms. It is
preferred to use methanol. It is preferred to perform the
full three washings with hot water, followed by the full
three washings with the alcohol.
After completion of the last step of the third wash
sequence, the final coated product is dried. Drying of the
product can be effected by any one of air drying at room or
elevated temperature, vacuum drying, washing with acetone,
or a combination of the above. It is preferred to first wash
the product with acetone, followed by drying at room
temperature.
The process of the present invention may be more fully
understood with reference to the accompanying drawings and
the following process description.
According to Figure l, non-noble metal substrate
20 material entering in line l is first pretreated, as
required, depending on the nature of the substrate, for
subsequent plating with noble metal. Where the nature of the
substrate material is such that it does not require
pretreating in the form of activation to remove any oxide
25 coating; seeding with atoms of another metal which is more
readily coated to facilitate plating; or mixing with
detergent to improve the uniformity of the plated noble
metal on the substrate material, the substrate material from


13398iû



line lis sent directly to the first plating solution bath
in line 24.
Where, however, the nature of the substrate material is
such that it readily forms an oxidized layer on its outer
surface, such as is the case with an aluminum powder
substrate, the substrate must first be activated by
treatment in activation step 3. The substrate material is
sent to the activation step in line 2. The chemicals used
to activate the metal generally include an aqueous solution
of an alkali metal cyanide supplied in line 4, and sodium
hydroxide supplied in line 5. A small amount of detergent
may also be added to help clean, degrease and deoxidize the
substrate in step 3. The activated substrate leaving the
activation step 3 in line 6 is then washed in step 7
15 with water supplied in line 8.
It has been found that most substrates which require
activation also coat better when mixed with a small amount
of a detergent prior to immersion in the plating solution
baths. The washed, activated substrate in line 9 is then
20 sent via lines 10 and 11 to detergent mixing step 21
to be mixed with detergent. Even where the substrate
material does not require activation because an oxidation
layer does not readily form on its outer surface, it has
been found that it may nevertheless be desirable to mix a
25 small amount of detergent with the substrate in order to
promote more uniform plating. Thus, substrate entering in
line 1, may alternatively be sent via line 20 to
detergent mixing step 21 to be directly mixed with some


133q-~10
-26-



detergent supplied in line 22 to form a paste of the
substrate material supplied from line 1 and the detergent
supplied from line 23. The substrate-detergent paste in
line 23 is then sent to plating via line 24. If it is
not desired to mix the washed activated substrate material
from line 10 with detergent before plating, the detergent
mixing step 21 can be bypassed using bypass line 12 and
the washed substrate from line 10 can be sent directly to
the first plating solution bath via line 24.
For certain substrate materials, particularly aluminum,
it has been found that plating with the noble metal proceeds
better when the substrate has been seeded with atoms of
another metal for which the noble metal has a greater
affinity. Thus, in the case of an aluminum substrate, it has
been found that noble metal coating is much improved when
the aluminum substrate has been seeded with atoms of copper.
For such cases, the activated and washed substrate material
leaving the washing step 7 by line 9 is seeded in
seeding step 14 with atoms of the seeding material
introduced in the form of a seeding solution in line 15
prepared in seeding solution preparation step 16. The
atoms of the seeding material are introduced through line
15 in the form of a water soluble salt of the seeding
material, such as copper sulfate, for the case where the
seeding material is copper atoms. Water is supplied by line
18. Additionally, ammonium hydroxide and potassium cyanide
can be added to the seeding solution to maintain the atoms
of the seeding material free in solution.


1339810
-27-



Referring to Fig. 2, a master plating solution is
prepared by determining the total requirement of noble metal
to be plated based on a consideration of the desired weight
percent of noble metal on the final coated product and the
5 weight of substrate material to be coated. Accordingly, the
desired amount of noble metal-containing compound in the
form of a cyanide, chloride or nitrate salt of the noble
metal, or preferably, an oxide of the noble metal, is sent
to master plating solution preparation step 25 via line
10 26, where it is mixed with water entering in line 28.
Where the noble metal compound utilized is the cyanide,
chloride, or oxide form, which generally range in being from
only slightly soluble to insoluble in aqueous solution, an
amount of an alkali metal cyanide, such as potassium or
15 sodium cyanide, is added to pro~ote dissolution of the noble
metal-containing compound, and to keep the ions of noble
metal supplied by the dissolved salt or oxide free in
solution. The cyanide, chloride and oxide compound forms of
noble metal are generally significantly more soluble in
20 cyanide-containing solutions. The alkali metals, which are
soluble in water, readily dissolve to supply the cyanide
ions in the aqueous solutions, which in turn enable the
noble metal containing compounds to dissolve more easily.
The use of an alkali metal cyanide, however, is not
25 recommended where the noble metal is gold. Where the noble
metal is supplied in the form of a nitrate salt of the noble
metal, the addition of little or no alkali metal cyanide is
required, since the nitrate salts are generally more soluble


1 3398 1 0
-28-



in aqueous solution than the other forms. Where the noble
metal to be plated is gold, supplied in any of the forms of
gold compound utilizable according to the process of this
invention, dissolution of the gold-containing compound is
5 promoted by the addition to the aqueous solution of an
amount of at least one of ammonium chloride, sodium citrate
and sodium hypophosphate. Preferably, a mixture of all three
is added to the gold compound/water plating solution bath to
promote dissolution of the gold compound. A mixture
10 containing ~he three in a weight ratio of ammonium chloride
to sodium citrate to sodium hypophosphate of from about 7.0
- 8.0 : 4.5 - 5.5 : 1 is most preferred. When utilized in
this ratio, the weight of sodium hypophosphate utilized is
from about 2.0 - 2.5 times the weight of the gold-containing
15 compound.
Individual plating solution baths are then prepared from
the master plating solution. A determination of the optimum
number of individual plating solution baths, ranging from 2
to 5, for the given combination of substrate material and
20 noble metal being plated is first made. For the plating of
silver or gold onto a copper substrate over the range of
weight percent of noble metal in the final coated product
according to this invention, it has been found that the use
of a full five plating solution baths results in the best
25 product. For the case of plating silver or gold onto a
nickel substrate over the range of weight percent of noble
metal in the final coated product according to the
invention, it has been found that four plating solution


1 3398 1 0
-29-



baths produces optimum coated product. For the plating of
silver or gold onto a copper-seeded aluminum substrate over
the range of weight percent of noble metal in the final
coated product according to the invention, it has been found
5 that two plating solution baths are sufficient to
consistently produce high quality coated product. The
optimum concentration of each plating solution bath is then
determined. The portion of the total amount of noble metal
being plated onto the substrate to be plated in each of the
10 determined number of baths ranges from a fraction of a
percent to approximately 80 percent, depending on the nature
of the noble metal and substrate materials and the number of
plating steps. Thus, in the case of plating silver or gold
onto copper, where it has been determined that five plating
15 solution baths provides optimum coating, it has further
been determined that the first bath should contain
approximately 80 percent of the total dissolved noble metal
ions from the master plating solution; the second bath
should optimally contain approximately 16 percent of the
20 total weight; the third bath should contain approximately
3.2 percent of the total weight; and the fourth and fifth
plating steps are reserved as final "touch-up" plating
steps, with each containing about 0.4 percent of the total
weight of noble metal ions in the master plating solution.
25 For the cases of plating silver or gold onto nickel or
copper-seeded aluminum substrates, it has been found that
equal division of the total amount of noble metal ions in
the master plating solution amongst the optimum number of


-30- 1 3398 1 0

individual plating solution baths results in coated product
having excellent properties. Thus, in the case of plating
silver or gold onto a nickel substrate, each of the four
baths preferable contains 25 percent of the total noble
metal free ions from the master plating solution. In the
case of plating silver or gold onto a copper-seeded
substrate, each of the optimum two individual plating
solution baths each contains 50 percent of the total noble
metal ions in the master plating solution. The above
examples of particular optimum conditions for several cases
of coated materials prepared according to the process of
this invention are not intended to be limiting. The process
of the invention generally produces consistently high
quality coated product over a broad range of combinations of
the number of plating solution baths and their individual
concentrations for all cases of substrate material and noble
metal. Other optimum combinations of parameters are readily
determinable by those skilled in the art.
With this in mind, the master plating solution in line
29 is divided into from two to five individual plating
solution bath feedstocks in lines 30, 31, 32, 33, 34,
which are sent to the respective first through fifth plating
solution bath preparation steps 35, 36, 37, 38, 39.
Water is added to each of the baths via lines 40, 41, 42,
43, 44, respectively, to increase the volume of the
solution and bring it to the proper concentration for
plating.
The substrate material, which may have been pretreated

1 33981 0



as required, according to the steps in Fig. 1, previously
described, enters the first plating solution bath via line
24, where coating of the noble metal in that solution is
effected until the plating solution is substantially
depleted of free noble metal ions. The intermediately plated
product, prepared in the first plating solution bath, leaves
through line 45 and is then separated from the lean
plating solution liquor in separation step 46. The lean
plating solution liquor is sent to appropriate waste
treatment or disposal via line 47.
The intermediately plated substrate material leaves the
separation step in line 48 and is then treated with a
first rinse sequence of steps 49. The coated substrate in
line 48 is sent to a first water rinse step 50, where it
is washed with water supplied in line 51. The rinsed
coated substrate material is separated and leaves in line
53. The rinse water is removed in line 52 and is sent to
appropriate waste treatment or disposal. The coated
substrate in line 53 is then sent to a second water rinse
step 54, where it is washed a second time with water
entering in line 55. The rinsed coated substrate material
is separated and leaves in line 57. The second rinse water
is removed via line 56 and is also sent to appropriate
waste treatment or disposal.
The washed, intermediately plated substrate from the
first plating step is then sent in line 58 to the second
plating solution bath 36, where further plating of the
substrate material occurs until the second plating solution


-32- 1 3 3 9 81 q



is substantially depleted of noble metal ions. The further
plated substrate material and lean plating solution liquor
are then removed from the second plating bath in line 59
and separated in separation step 46, which is repeated
exactly as described above following the first plating step.
The two steps 50,54 of the first rinse sequence 49 are
then also repeated for the further coated substrate from the
second plating step. The washed, further coated substrate
material leaves in line 57.
Depending on whether there are any additional third
through fifth plating steps remaining, the substrate
material is sequentially sent to such respective plating
solution baths 37, 38, 39, via lines 60, 62, 64,
respectively. The further coated substrate material and lean
15 plating solution liquor substantially depleted of free noble
metal ions from each of the third through fifth plating
steps, is removed from the respective bath in lines 61, 63,
65 and sent to separation step 46 and steps 50 and 54
of first rinse sequence 49, where the separation of the
20 substrate from the lean liquor and the two water rinsing
steps are respectively performed.
After completion of the above sequence for the final
plating step, the final plated substrate is sent to the
second rinse sequence in line 66.
According to Fig. 3, the final coated substrate material
from the water rinse step 54 of first rinse sequence 49
following completion of the last plating step is sent in
line 66 to second rinse sequence 67, where the four


133~8lo

-33-




separate rinse steps 68, 72, 76, 80 of the sequence are
sequentially performed.
The substrate material in line 66 is first washed with
water in first water rinse step 68. Rinse water is
supplied in line 69. The rinse water is separated from the
coated material and is sent to appropriate waste treatment
or disposal in line 70. The washed coated substrate
material in line 71 is then washed with a weak acid in
acid rinse step 72. The weak acid, preferably a 25% by
volume aqueous glacial acetic acid solution, is supplied in
line 73. The acid solution is separated from the coated
material and is sent to appropriate waste treatment or
disposal in line 74. The acid-washed coated substrate
material in line 75 is then washed a second time with
water in second water rinse step 76. Rinse water is
supplied via line 77. The rinse water is separated from
the coated material and is sent to appropriate waste
treatment or disposal in line 78. The water-washed coated
substrate material leaving the second water rinse step in
line 79 is finally washed with an alcohol in alcohol rinse
step 80. The alcohol, containing from 1-4 carbon atoms,
preferably methanol, is supplied in line 81. The alcohol
is separated from the coated material and is sent to
appropriate waste treatment or disposal in line 82. The
complete four-step second rinse sequence is performed a

total of from one to four times. Recycle line 84
represents the repetition of the second rinse sequences. The


1339810
-34-



final washed coated substrate after alcohol rinse leaving in
line 83 is returned to the first water rinse step 68 and
the entire sequence as just described is repeated the
desired number of times. Preferably, the sequence is
performed a total of four times. The final washed coated
product material after completion of the last step of the
last repetition of the second rinse sequence is then sent,
in line 85, to the third rinse sequence 86, where a two
step sequence of washing the final coated substrate material
first with water, in water rinse step 87, followed by
washing with alcohol, preferably methanol, in alcohol rinse
step 92, is performed. The alcohol is separated and
withdrawn in line 95. Both the water rinse step of the
sequence and the alcohol rinse step of the sequence can each
I5 be performed from one to three times. All water rinse steps
are completed before the alcohol rinse step or steps are
performed. The provision for repetition of the washing steps
is shown by recycle lines 90 and 95, respectively.
The final coated product in line 96, after completion
of the last rinse step of the third rinse sequence, is
lastly sent to drying step 87, where the final, washed
coated substrate material is dried by one of physical means,
such as air drying or vacuum drying; or by chemical means,
such as by washing with acetone; or by a combination of
25 those methods. The physical or chemical drying agent, if
such is utilized, is introduced into the drying step via
98.
The final washed, coated product 96 is then dried

1 339~ 1 0
-35-



according to any one of various drying steps, and is
withdrawn in line 99 as the final washed, coated product.
It will be apparent to those skilled in the art that the
process of this invention can readily be carried out in a
plurality of ways, including on a batch, semi-batch or
continuous basis, utilizing appropriate equipment in each
case. Similarly, the scale of production of coated product
is flexible, ranging from the order of magnitude of several
grams of product on a semi-micro scale to several hundreds
of pounds on a commercial scale. The particular manner of
carrying out the process is generally determined in part by
the scale of the operation, with semi-micro scale quantities
generally being produced on a batch or semi-batch basis and
commercial scale quantities being produced on a larger
semi-batch or continuous processing basis. It will be
further apparent to those skilled in the art that while the
foregoing process description is written for a commercial
scale semi-batch basis, the steps are identical for other
bases, although the equipment utilized will be different and
not as complex. ThuS, for example, in production on a batch
basis, separation of coated product from lean plating
solution liquor may occur by simple decantation of the
liquor from the coated substrate in the plating vessel,
which may simply be a beaker. Similarly, on a batch basis,
25 reference in the foregoing process description to transport
of the various materials through numbered lines will be
understood generally to simply represent the act of pouring
or mixing the indicated components.


~ 3398 1 0
-36-



The coated substrates produced in accordance with the
foregoing have utility in a wide variety of applications
requiring electrically conductive materials or
electromagnetic interference shielding materials. Because of
the superior physical and electrical properties of
electrically conductive noble metal coated non-noble metal
substrate powders produced in accordance with the present
process, it has been found that the properties and
functional performance of the conductive materials and
shielding materials incorporating such coated powders are
surprisingly significantly superior to those of similar
materials fabricated utilizing noble metal coated non-noble
metal powders produced according to previously known
methods.
When used in the fabrication of electromagnetic
interference shielding materials, the coated powder produced
according to the present process are incorporated into a
resin or plastic matrix. The materials have a composition of
from about 80 - 90 weight percent coated powder and from
about 10 - 20 weight percent matrix material.
The matrix material in which the noble metal coated
non-noble metal substrate powder is dispersed can be a
rubber, a plastic material, an elastic material, or a
mixture of such materials. Preferred types of elastic
25 materials include silicone, fluorosilicone, and
polyisobutylene elastomers. Preferred types of plastic
materials include polyamides, acrylics, urethanes and
polyvinyl chloride silicone plastic. Electromagnetic


1339810
-37-



interference shielding materials wherein the noble metal
coated non-noble metal is aluminum seeded with copper and
coated with silver, or is silver or gold on a nickel
substrate, are new.
Other types of useful electrically conducting materials
utilizing the noble metal coated, non-noble metal substrate
powders produced according to the present process include an
electrically conducting thermosetting plastic based on
polyamine and diisocyanate; an electrically conductive
material based on a copolymer matrix of at least one
compound of chlorinated biphenyl and triphenyl, amorphous
polypropylene, ethylene, vinyl acetate, phenol,
formaldehyde, and terpine; an electrically conductive
adhesive material based on chlorinated biphenyl and
triphenyl, and amorphous polypropylene; and an electrically
conductive material based on polyamide resin and epoxy.



The features of this invention may be more fully
understood with reference to the following non-limiting
examples which set forth particularly preferred embodiments
20 of the process of preparing the coated materials and
compositions utilizing them.


1 3398 1 0
-38-



EXAMPLES



The following are representative examples of the process
for preparing noble metal plated non-noble metal substrate
powders and electrically conductive compositions
incorporating such powders, according to the invention.
These examples are not intended to be limiting of the range
of such materials which can be prepared according to the
invention. Other examples within the scope of the claims
will be readily apparent to those skilled in the art.



Example 1 - Plating Silver Onto Copper Powder



The process for plating silver onto copper powder according
to the present invention comprises the following steps:



a) Preparation of Starter Plating Solution
A starter plating solution containing free silver ions
was prepared by first dissolving 2600 g. of potassium
cyanide in 15 1. of boiling water, contained in a first

enamel- lined kettle. To this was added 1300 g. of silver
oxide (1210.3 equivalent g. silver) with constant stirring
until dissolved.



b) Preparation of Plating Solution Baths
Five plating solution baths were prepared from the
starter plating solution. Into a second enamel-lined kettle


1 33981 0

-39-



was poured 0.8 (12 1.) of the volume of solution in the
first kettle. Hot water (3 1.) was added to raise the volume
to 15 1. This became the first plating solution bath, having
a free silver concentration of 64.55 g./1. and supplying an
equivalent weight of 968.2 g. of silver as free silver ions
available for plating.
The remaining 0.2 (3 1.) of the volume of starter plating
solution in the first kettle was raised to 15 1. by the
addition of 12 1. of hot water. Into a third enamel-lined
kettle was then poured 0.2 (3 1.) of the volume of solution
in the first kettle. The remaining 0.8 (12 1.) of the
volume of solution in the first kettle became the second
plating solution bath, having a free silver concentration of
16.4 g.~l. and supplying an equivalent weight of 193.7 g. of
silver as free silver ions available for plating.
Hot water (12 1.) was added to the volume (3 1.) of
solution in the third kettle to raise the volume to 15 1.
Into each of a fourth and fifth enamel-lined kettle was
poured 0.1 (1.5 1.) of the volume of solution in the third
kettle. The remaining 0.8 (12 1.) of the volume of solution
in the third kettle became the third plating solution bath,
having a free silver concentration of 3.23 g./l. and
supplying an equivalent weight of 38.7 g. of silver as free
silver ions available for plating.
Hot water (13.5 1.) was added to the 1.5 1. of solution
in each of the fourth and fifth kettles. These solutions
became, respectively, the fourth and fifth plating solution

~ 33981 0
-40-



baths, each having a free silver concentration of 0.32 g./l.
and each supplying an equivalent weight of 4.85 g. of silver
as free silver ions available for plating.



c) Plating of Copper Powder with Silver
The first of five plating steps was performed by stirring
5670.0 g. of copper powder, having spherical shaped
particles averaging 10 microns in diameter, into the first
plating solution bath, maintained at a temperature around 68
to 70 C, to effect plating of the free silver ions in the
10 bath onto the surface of the copper powder. When the first
plating solution bath was substantially depleted of silver
ions, the lean liquor was decanted from the powder and the
intermediately plated copper powder (14.6 weight % silver)
was first rinsed once with warm water, followed by a rinse
15 with hot water.
The second plating step was performed by immersing the
intermediately plated copper powder into the second plating
solution bath, maintained at a temperature of from
85 to 95 C, to further plate the powder with the free
20 silver ions contained therein. When the second plating
solution bath was substantially depleted of silver ions, the
lean liquor was decanted from the powder and the further
intermediately plated copper powder (17.0 weight % silver)
was rinsed with warm and hot water, as after completion of
25 the first plating step.

The same procedure, including the post-plating rinse

1 33981~
-41-



sequence of steps of rinsing in succession with warm and hot
water, as performed above for the first and second plating
steps with the first and second plating solution baths, was
then repeated for the third plating step using the third
plating solution bath.
After the rinsing sequence following the third plating
step, the intermediately plated copper powder (17.5 weight %
silver) was rinsed once with a second series of rinses which
included the sequence of steps of rinsing the powder once
with hot water, rinsing once with a 25% glacial acetic acid
aqueous solution, rinsing a second time with hot water, and
finally rinsing once with methanol.
After completion of the second series of rinses, the
fourth plating step was performed by immersing the
intermediately plated copper powder in the fourth plating
solution bath, maintained at a temperature of from 85 to
95 ~C, to further p1ate the copper powder with the silver
ions contained in the fourth plating solu'ion bath. When the
fourth plating solution bath was substantially depleted of
20 silver ions, the lean liquor was decanted, and the still
further intermediately plated copper powder (17.53 weight %
silver) was rinsed first with warm water, followed by a
rinse with hot water, as after previous plating steps.
The final, fifth plating step, including a post-plating
25 sequence of steps of rinsing in succession with warm and hot
water, was then performed following the same procedure as
with previous plating steps, utilizing the fifth plating


-42- ~33981~

solution bath, to produce the final plated powder, having a
silver content of 17.6 weight % of the total weight.



d) Post-Plating Rinsing of Final Plated Powder
After completion of the post-plating warm and hot water
rinses following the fifth plating step, a second series of
rinse steps, including the sequence of rinsing the final
plated powder a first time with hot water rinsing once with
a 25% glacial acetic acid aqueous solution; rinsing a second
time with hot water; and rinsing once with methanol, was
performed four times in succession.
After completion of the fourth repetition of the second
rinse series following the fifth plating step, the final
plated powder was further rinsed with a third series of
rinse steps, which included rinsing the powder 3 times in
succession with hot water, followed by rinsing 3 times in
succession with methanol.
The plated, rinsed powder was then allowed to air dry to
produce the final plated product.




Example 2 - Plating Silver Onto Nickel Powder



20 The process for plating silver onto nickel powder according

to the present invention comprises the following steps:



a) Preparation of Starter Plating Solution

133981()

-43-



A starter plating solution containing free silver ions
was prepared by first dissolving 2240 g. of potassium
cyanide in 15 1. of boiling water, contained in a first
enamel-lined kettle. To this was added 1164 g. of silver
oxide (1083.6 equivalent g. silver) with constant stirring
until dissolved.



b) Preparation of Plating Solution Baths
Four plating solution baths were prepared from the
starter plating solution. Into each of second, third and
fourth enamel-lined kettles was poured 0.25 (3.75 1.) of the
starter plating solution, leaving 0.25 of the solution in
the first kettle. Hot water (11.25 1.) was added to each of
the four kettles to raise the volume in each to 15 1. Each
of the four plating solution baths had a free silver
15 concentration of 18.06 g./l. and supplied an equivalent
weight of 270.9 g. silver as free silver ions available for
plating.



c) Cleaning and Activation of Nickel Powder
Nickel powder (5670.0 g.) having spherical shaped
20 particles averaging 10 microns in diameter was cleaned and
activated to remove any grease, dirt and oxide coating on

its outer surface which would interfere with plating, before
commencement of the first plating step, by first mixing the
nickel powder with liquid detergent to form a paste and then
25 washing the powder paste with an activation solution made by

~ 33981~

-44-



dissolving 400 g. of potassium cyanide in 7.5 1. of boiling
water (53.3 g./l.). Appearance of a dark foam indicated
removal of the oxide coating on the outer surface of the
powder. When foaming ceased, the activation solution was
5 decanted and the cleaned, deoxidized nickel powder was
rinsed twice with hot water. After rinsing, a small amount
(75-100 ml.) of liquid detergent was mixed with the powder.



d) Plating of Nickel Powder with Silver
The first of four plating steps was performed by stirring
10 the cleaned and activated nickel powder into the first
plating solution bath, maintained at a temperature
of from 50 to 80 ~C, preferably close to 74 ~C, to
effect plating of the free silver ions in the bath onto the
surface of the powder. When the first plating solution bath
15 was substantially depleted of silver ions, the lean liquor
was decanted from the powder and the intermediately plated
nickel powder (4.6 weight ~ silver) was rinsed twice in
succession with hot water.
The second through fourth plating steps were then
20 performed following the same procedure of the first plating
step, including the sequence of rinsing twice with hot water
after each plating step. The only difference with the second
through fourth plating steps was that the plating solution
bath temperature for these plating steps was higher. The

25 temperature of the subsequent plating solution baths was
maintained at a temperature of from 85 - 95 ~C, in


1 33981 0



comparison to the S0 - 80 C temperature of the first
bath. After the second, third and fourth plating steps, the
nickel powder was coated with 8.7, 12.5 and 15.8 weight %
silver, respectively.



5 e) Post-Plating Rinsing of Final Plated Powder
After completion of the post-plating two hot water
rinses, a second series of rinse steps, including the
sequence of rinsing the final plated powder a first time
with hot water; rinsing once with a 25% glacial acetic acid
10 aqueous solution; rinsing a second time with hot water; and
rinsing once with methanol, was performed a total of four
times in succession.
After completion of the fourth repetition of the second
rinse series following the fourth plating step, the final
15 plated powder was further rinsed with a third series of
rinse steps, which included rinsing the powder with three
consecutive hot water rinses, followed by three consecutive
rinses with methanol.
The second and third series of rinse steps, therefore,
20 was identical to the second and third series performed for
the preparation of silver coated copper powder, as in step
(d) of Example 1, above.
The plated, rinsed powder was then allowed to air dry to
produce the final plated product.


1339810

-46-



Example 3 - Plating Silver Onto Copper-Seeded Aluminum
Powder



The process for plating silver onto copper-seeded aluminum
powder according to the present invention comprises the
following steps:



a) Preparation of Starter Plating Solution
A starter plating solution containing free silver ions
was prepared by first dissolving 990 g. of potassium cyanide
in 15 1. of boiling water, contained in a first enamel-lined
kettle. To this was added 495 g. of silver oxide (460.8
equivalent g. silver) with constant stirring until
dissolved.



b) Preparation of Plating Solution Baths
Two plating solution baths of identical concentration
15 were prepared from the starter plating solution. Into a
second enamel-lined kettle was poured 0.5 (7.5 1.) of the
starter plating solution, leaving the remaining half in the
first kettle. Hot water (7.5 1.) was added to each of the

kettles to raise the volume in each to 15 1. Each of the two
20 plating solution baths had a free silver concentration of
15.36 g./l. and supplied an equivalent weight of 230.4 g.
silver as free silver ions available for plating.


1339810



c) Preparation of Copper Seeding Solution
A solution for seeding copper atoms into the aluminum
powder to be coated was prepared by dissolving 220.0 g. of
copper sulfate (87.6 equivalent g. copper) in one gallon of
cold water. The resulting solution was clear blue in color.
To this solution was then added approximately 300 ml.
ammonium hydroxide until the color of the solution became
dark blue. Finally, approximately 178 g./l. of potassium
cyanide solution was added to the copper solution. The
10 resulting final copper seeding solution was transparent
yellow in color.



d) Cleaning and Activation of Aluminum Powder
Aluminum powder (1816.0 g.) having spherical shaped
particles averaging 10 microns in diameter was cleaned and
15 activated to remove any grease, dirt and oxide coating on
its outer surface which would interfere with plating, before
commencement of the first plating step, by placing the
aluminum powder in a container holding 10 liters of water.
Sodium hydroxide (10.0 g.) was added with constant stirring.
20 A froth evolving reaction occurred indicating cleaning and
deoxidation of the aluminum powder was occurring. Stirring
was maintained until cessation of the frothing reaction,
which indicated that the aluminum powder was completely
clean and activated. The sodium hydroxide solution was
25 decanted and the activated aluminum powder was rinsed with
cold water.


8 i 0


-48-



e) Seeding of Aluminum Powder with Copper
The cleaned and activated aluminum powder was the seeded
with copper atoms by adding the copper seeding solution
prepared in step (c), above, to the cleaned and activated
5 aluminum powder prepared in step (d), above, with stirring.
Copper atoms precipitated from the seeding solution to seed
the aluminum powder. The resulting copper seeded aluminum
powder became reddish in color. The lean copper seeding
solution was then decanted and the copper-seeded aluminum
10 powder was rinsed with cold water.



f) Plating of Copper-Seeded Aluminum Powder with Silver
In order to further facilitate the plating of silver onto
the copper- seeded aluminum powder and to promote the
production of high quality coated product having a high
15 luster, liquid detergent was added to the powder before
commencing the first plating step.
The first plating step was then performed by adding
1903.6 g. of copper-seeded aluminum powder, to which the
liquid detergent had just been added, into the first plating
20 solution bath, maintained at a temperature of around 32 C,
to effect plating of the free silver ions in the bath onto
the surface of the powder. ~hen the first plating solution
bath was substantially depleted of silver ions, the lean

liquor was decanted from the powder and the intermediately
25 plated powder (10.8 weight % silver) was rinsed twice in
succession with cold water.


-49- 1 33981 0


The second plating step was then performed by immersing
the intermediately plated powder into the second plating
solution bath, maintained at a temperature of from 60 - 70
~C, preferably 65 ~C, to further plate the copper-seeded
aluminum powder with the free silver ions contained therein.
When the second plating solution bath was substantially
depleted of silver ions, the lean liquor ~as decanted from
the powder and the final coated copper-seeded aluminum
powder, having a silver content of 19.5 weight ~ of the
10 total weight, was rinsed twice in succession with cold water
as after the first plating step.



g) Post-Plating Rinsing of Final Plated Powder
After completion of the second cold water rinsing step
following the final plating step, second and third series of
15 rinse steps, identical to those performed in Examples 1 and
2, above, were performed.
The plated, rinsed copper-seeded aluminum powder was then
allowed to air dry to produce the final plated product.




Example 4 - Plating Gold Onto Nickel Powder




A coating of gold is plated onto a nickel powder
substrate substantially in accordance with the four-step
plating process of Example 2 with the following
modifications. The steps of the process include:


~ 3~;9~

so--

a) Preparation of Starter Plating Solution
A starter plating solution containing free gold ions is
prepared by first dissolving 1110 g. of ammonium chloride,
740 g. of sodium citrate and 150 g. of sodium hypophosphate
in 15 1. of boiling water, contained in a first enamel-lined
kettle. To this was added 64 g. of potassium gold cyanide
(43.8 equivalent g. gold) with constant stirring until
dissolved.



b) Preparation of Plating Solution Baths
Four plating solution baths are prepared from the starter
plating solution. Into each of second, third and fourth
enamel-lined kettles is poured 0.25 (3.75 1.) of the starter
plating solution, leaving 0.25 of the solution in the first
kettle. Hot water (11.25 1.) is added to each of the four
15 kettles to raise the volume in each to 15 1. Each of the
four plating solution baths has a free gold concentration of
0.73 g./l. and supplies an equivalent weight of 10.95 g.
gold as free gold ions available for plating.



c) Cleaning and Activation of Nickel Powder
Nickel powder (230.0 g.) having spherical shaped
particles averaging 8-10 microns in diameter is cleaned and
activated to remove any grease, dirt and oxide coating on
its outer surface which would interfere with plating, before

commencement of the first plating step, by following the
25 procedure described above in step (c) of Example 2.

-51- 1339810

d) Plating of Nickel Powder with Gold
The first of four plating steps is performed by stirring
the cleaned and activated nickel powder into the first
plating solution bath, maintained at a temperature
5 of from 50 to 80 C, preferably close to 74 C, to
effect plating of the free silver ions in the bath onto the
surface of the powder. When the first plating solution bath
is substantially depleted of gold ions, indicated by the
solution turning greenish in color and the nickel powder
10 turning gold in color, the lean liquor is decanted from the
powder and the intermediately plated nickel powder (4.5
weight % gold) is rinsed twice in succession with hot water.
The second through fourth plating steps are then
performed following the same procedure of the first plating
15 step, including the sequence of rinsing twice with hot water
after each plating step. The only difference with the second
through fourth plating steps is that the plating solution
bath temperature for these plating steps is higher. The
temperature of the subsequent plating solution baths is
20 maintained at a temperature of from 90 - 98 ~C, in
comparison to the 50 - 80 C temperature of the first
bath. Care must be taken that the solution does not reach
the boiling point, however, because the volume of a boiling
solution increases 250 percent upon introduction of the
25 nickel powder, due to excessive frothing. After the second,
third and fourth plating steps, the nickel powder was coated
with 8.7, 12.5 and 16.0 weight % gold, respectively.


' -52- l 339 8 l O

e) Post-Plating Rinsing of Final Plated Powder
After completion of the post-plating two hot water
rinses, the second and third series of rinse steps are
performed identically as described above in step (e) of
5 Example 2 for the rinsing of silver-coated nickel powder.
Finally, the plated, rinsed powder is allowed to air dry
to produce the final plated product.



Example 5 - Preparation of an Electromagnetic Interference
Shielding Material Containing Silver-Coated Copper Particles



A silicone rubber-based electromagnetic interference
shielding material containing silver-coated copper powder
particles is prepared by mixing 34.0 g. of a silicone rubber
gum, such as #440 silicone rubber gum manufactured by Dow
Corning Corp., Midland, Michigan, with 0.3 g. of
15 (2,5-dimethyl, 2,5-di-t-butyl-peroxy) hexane, such as is
sold under the tradename Varox, manufactured by R.T.
Vanderbilt Co., and 3.7 g. of silica, such as CAB-O-SIL MS7
silica, with 238.0 g. of approximately 17 weight percent
silver plated onto copper powder particles prepared
20 according to the process of Example l, above. The mixture is
blended to homogeneity in a mill mixer. The mixture is then
molded into parts or rolled into sheet at
a temperature of around 325 F, and under a pressure of
approximately 30 tons, for from 14 - 20 minutes. The molded
25 parts are then post cured at a temperature of




*Trademarks

-53- 1339810

around 350 F for 3 hours. The final shielding material
has a composition of 86.2 weight percent silver coated
copper powder particles.



Example 6 - Preparation of an Electromagnetic Interference
5 Shielding Material Containing Silver-Coated Copper Particles



An electromagnetic interference shielding material
containing silver-coated copper powder particles is prepared
by mixing 11 parts by weight of epoxy with 89 parts by
weight of silver-coated copper powder particles prepared
10 according to the process of Example 1, above, but wherein
the coated copper particles contain from 5 - 8 weight
percent silver, and wherein the silver coated copper
particles added to the epoxy are sized such that 85% pass
through a 200 mesh screen.




15 Example 7 - Preparation of an Electromagnetic Interference
Shielding Material Containing Silver-Coated Nickel Particles



A silicone rubber-based electromagnetic interference

shielding material containing silver-coated nickel powder
particles is prepared by mixing 0.0978 parts by weight of a
20 silicone rubber gum, such as #440 silicone rubber gum
manufactured by Dow Corning Corp., Midland, Michigan, with
0.0008635 parts by weight of (2,5-dimethyl,


133~81~

2,5-di-t-butyl-peroxy) hexane, such as is sold under the
tradename Varox, manufactured by R.T. Vanderbilt Co., and
0.0106505 parts by weight of silica, such as CAB-O-SIL MS7
silica, with 0.6846 parts by weight of approximately 15
5 weight percent silver plated onto nickel powder particles
prepared according to the process of Example 2, above. The
mixture is blended to homogeneity in a mill mixer. The
mixture is then molded into parts or rolled into sheet at
a temperature of around 325 F, and under a pressure of
10 approximately 30 tons, for from 14 - 20 minutes. The molded
parts are then post cured at a temperature of
around 350 F for 3 hours. The final shielding material
has a composition of 86.2 weight percent silver coated
nickel powder particles.




15 Example 8 - Preparation of an ~lectromagnetic Interference
Shielding Material Containing Silver-Coated Aluminum
Particles



A silicone rubber-based electromagnetic interference
shielding material containing silver plated aluminum powder
20 particles is prepared by mixing 34.0 g. of a silicone rubber
gum, such as #440 silicone rubber gum manufactured by Dow
Corning Corp., Midland, Michigan, with 0 3 g. of
(2,5-dimethyl, 2,5-di-t-butyl-peroxy) hexane, such as is

sold under the tradename Varox, manufactured by R.T.


1 3398 1 0


Vanderbilt Co., and 3.7 g. of silica, such as CAB-0-SIL MS7
silica, with 63.0 g. of approximately 20 weight percent
silver plated onto copper-seeded aluminum powder particles
prepared according to the process of Example 3, above. The
5 mixture is blended to homogeneity in a mill mixer. The
mixture is then molded into parts or rolled into sheet at a
temperature of around 325 F, and under a pressure of
approximately 30 tons, for from 14 - 20 minutes. The molded
parts are then post cured at a temperature of around 350
10 ~F for 3 hours. The final shielding material has a
composition of 62.4 weight percent silver coated aluminum
powder particles.




Example 9 - Preparation of an Electrically Conductive
Resin-Based Material Containing Silver-Coated Nickel
15 Particles



An electrically conductive resin-based material
containing gold- coated nickel powder particles is prepared
by mixing from four to six parts by weight of a
silver-coated nickel powder prepared according to Example 2,
20 above, with one part by weight of an epoxy resin, such as is
commercially available under the tradename TITAN-TITE, a
clear epoxy resin, manufactured by Glass Plastic Corp.,

Linden, N.J.


*Trademarks

-56- l 3398 1 0

Example 10 - Preparation of an Electrically Conductive
Resin-Based Material Containing Gold-Coated Nickel Particles



An electrically conductive resin-based material
containing gold- coated nickel powder particles is prepared
5 by mixing from five to six parts by weight of a gold-coated
nickel powder prepared according to Example 4, above, with
one part by weight of the TITAN-TITE clear epoxy resin
described in Example 8, above.




Example 11 - Preparation of Electrically Conductive
10 Copolymer Materials Containing Silver Plated Nickel
Particles



Various electrically conductive copolymer materials
containing silver plated nickel powder particles are
prepared by first preparing a copolymer matrix composition
15 according to the following formulations:



a) Copolymer composition Parts by weight
ARCHLOR 5442 3 - 8

ARC~LOR 1254 1 - 5
EASTOBOND M-5H 1 - 6



20 ARCHLOR 5442 is the tradename of a chlorinated triphenyl
plastic manufactured by Monsanto Co., St. Louis, Mo. ARCHLOR



*Trademarks

~ '~
133q810
-57-



1254 is the tradename of a chlorinated biphenyl plastic
manufactured by Monsanto Co., St. Louis, Mo. EASTOBOND M-5H
is the tradename of an amorphous polypropylene plastic
manufactured by Eastman Chemical Products, Inc., Ringsport,
5 Tenn.



b) Copolymer compositionParts by weight
ARCHLOR 5442 2 - 7
ARCHLOR 1254 2 - 6
EASTOBOND M-5H 1.5 - 5
ELVAX 150 1.5 - 6



ELVAX 150 is the tradename of a copolymer composed of 67
weight percent ethylene and 33 weight percent vinyl acetate,
manufactured by E.I. Du Pont de Nemours, Wilmington, Del.



~) Copolymer compositionParts by weight
ARCHLOR 5442 1.5 - 7
ARCHLOR 1254 2 - 6
EASTOBOND M-5H 1 - ~
SUPER BECKACITE 21001.5 - 4.5




SUPER BECKACITE 2100 is the tradename of a phenolic resin
20 copolymer composed of phenol, formaldehyde, and terpine,
manufactured by Reichhold Chemicals, Inc., White Plains,
N.Y.


*Trademarks

-58- 1339810

d) Copolymer composition Parts by weight
ARCHLOR 5442 5 - 7
ARCHLOR 1254 2 - 6
EASTOBOND M-5H 1 - 5
SUPER BECKACITE 2000 1.5 - 5



SUPER BECKACITE 2000 is the tradename of a phenolic resin
copolymer co-mposed of a terpine phenol polymer, made
Reichhold Chemicals, Inc., White Plains, N.Y.



e) Copolymer composition Parts by weight
ARCHLOR 5442 1.5 - 7
ARCHLOR 1254 2 - 6
EASTOBOND M-5H 1 - 5
SUPER BECKACITE 1050 1.5 - 5



SUPER BECKACITE 1050 is the tradename of a phenolic resin
15 copolymer composed of a phenol formaldehyde copolymer,
manufactured by Reichhold Chemicals, Inc., White Plains,
N.Y.



For all of the above copolymer matrix formulations, the
listed ingredients are placed in a pyrex glass container and

20 heated with constant stirring until the mixture becomes a
clear homogeneous liquid. The electrically conductive
materials are prepared by combining from 3 to 7 parts by
weight of silver coated nickel powder particles prepared


-59- l33~810

according to the process of Example 2, above, with l part by
weight of any of the above liquified copolymer compositions
(a) through (e).




Example 12 - Preparation of Electrically Conductive
5 Copolymer Materials Containing Gold Plated Nickel Particles



Various electrically conductive copolymer materials
containing gold plated nickel powder particles are prepared
by first preparing a copolymer matrix composition according
to any of the formulations designated (a) through (e) in
lO Example ll, above. The electrically conductive materials are
prepared by then combining from 3 to 7 parts by weight of a
gold coated nickel powder particles prepared according to
the process of Example 4, above, with l part by weight of
any of the above liquified copolymer compositions (a)
15 through (e).




Example 13 - Preparation of an Electrically Conductive
Thermoset Plastic Material Containing Silver-Coated Nickel
Particles




An electrically conductive thermosetting polyurea based
20 plastic material containing silver-coated nickel powder
particles is prepared as a two part formulation which is


-60- l 33981 0

combined at time of use as follows:
The first part of the formulation is prepared by mixing
0.84 parts by weight of a modified polyamine such as is
commercially available under the tradename AMINE-lO0,
5 manufactured by General Mills Chemicals, Kankakee, Ill.,
with 0.43 parts by weight of xylene solvent. To this is
added 3.8 parts by weight of silver-coated nickel powder
prepared according to the process of Example 2, above, to
form the first part of the thermosetting plastic material.
The second part of the formulation is prepared by mixing
1.26 parts by weight of diisocyanate, such as is
commercially available under the tradename D.D.I. 1410
manufactured by General Mills Chemicals, Kankakee, Ill.,
with 0.60 parts by weight of toluene solvent. To this is
15 added 6.3 parts by weight of silver-coated nickel powder
prepared according to the process of Example 2, above, to
form the second part of the thermoset'ing plastic material.
The first and second parts of the electrically
conductive tnermosetting plastic material are kept separate
20 until such time as it is desired to from the thermosetting
plastic material, when the first and second parts are mixed
in a 1:1 weight ratio to form the electrically conductive
thermosetting plastic material.


*Trademarks

-61- 1339810

Example 14 - Preparation of an Electrically Conductive
Thermoset Plastic Material Containing Gold-Coated Nickel
Particles



An electrically conductive thermosetting polyurea based
5 plastic material containing gold-coated nickel powder
particles is prepared in the same manner as is described in
Example 13, above, except that gold-coated nickel powder
particles prepared according to the process of Example 4,
above, are substituted for the silver-coated nickel powder
10 particles.




Example 15 - Preparation of an Electrically Conductive
Polyamide and Epoxy Based Plastic Material Containing
Silver-Coated Nickel Particles



An electrically conductive polyamide and epoxy based
15 plastic material containing silver-coated nickel powder
particles is prepared by mixing 0.5 parts by weight of a
polyamide resin which is the reaction product of linoleic
acid and polyamine, such as is commercially available under
the tradename VERSAMID 115, manufactured by General Mills
20 Chemicals, Kankakee, Ill., with 0.5 parts by weight of an

epoxy which is diglycidyl ether of bisphenol A, such as is
commercially available under the tradename GENEPOXY 190,
manufactured by General Mills Chemicals, Kankakee, Ill., and



*Trademarks

-62- 1 33~10

6 parts by weight of silver-coated nickel powder particles
prepared according to the process of Example 2, above.




Example 16 - Preparation of an Electrically Conductive
Polyamide and Epoxy Based Plastic Material Containing
5 Gold-Coated Nickel Particles



An electrically conductive polyamide and epoxy based
plastic material containing gold-coated nickel powder
particles is prepared in the same manner as is described in
Example 15, above, except that gold-coated nickel powder
10 particles prepared according to the process of Example 4,
above, are substituted for the silver- coated nickel powder
particles.




Example 17 - Preparation of an Electrically Conductive
Adhesive Material Containing Silver-Coated Nickel Particles



An electrically conductive adhesive material containing
silver-coated nickel powder particles is prepared by first
preparing a mixture containing from 2 to 6 parts by weight
of ARCHLOR 5442; from 3 to 7 parts by weight of ARCHLOR
1254; and from 1 to 6 parts by weight of EASTOBOND M-5H. The
20 above components are heated in a pyrex glass dish with
constant stirring until they liquify into a homogeneous


1 33981 0
-63-



clear liquid. From 3.5 to 6.5 parts by weight of
silver-coated nickel powder particles prepared according to
the process of Example 2, above, are added to 1 part by
weight of the above copolymer liquid, with constant
5 stirring. The resulting mixture is cooled allowing the
copolymer liquid to solidify into an adhesive consistency
with the silver-coated nickel powder particles distributed
throughout the adhesive composition. The final composition
has good to excellent electrical conductivity.




10 Example 18 - Preparation of an Electrically Conductive
Adhesive Material Containing Gold-Coated Nickel Particles



An electrically conductive adhesive material containing
gold-coated nickel powder particles is prepared by first
preparing the liquld copolymer mixture described above in
15 Example 11. From 4.5 to 7.0 parts by weight of gold-coated
nickel powder particles prepared according to the process of
Example 4, above, are added to l part by weight of the above
copolymer liquid, with constant stirring. The resulting
mixture is cooled allowing the copolymer liquid to solidify
20 into an adhesive consistency with the gold-coated nickel

powder particles distributed throughout the adhesive
composition. The final composition has good to excellent
electrical conductivity.


1 33981 0
-64-



Example 19 - Preparation of an Electrically Conductive
Adhesive Material Containing Silver-Coated Nickel Particles



An electrically conductive adhesive material containing
silver-coated nickel powder particles is prepared by first
preparing a mixture containing 76 parts by weight of
isooctyl acrylate, 20 parts by weight of
N-vinyl-2-pyrrolidone, 4 parts of acrylamide, and 0.04 parts
by weight of a photoinitiator, such as
2,2-dimethoxy-2-phenylacetophenone, as is available under
the tradename Irgacure 651, and then partially
photopolymerizing the mixture to a syrup having a viscosity
of about 2000 centipoise. To 85 parts by weight of this
syrup is added 15 parts by weight of silver plated nickel
particles prepared substantially in accordance with the
15 process of Example 2, above, but using flake-shaped nickel
particles, rather than the spherical shaped particles of
that example. To the particle-filled syrup is added 0.05
parts by weight of a crosslinking agent, such as hexanediol
diacrylate and an additional 0.1 part by weight of
20 photoinitiator. This mixture is then immediately coated
between two silicone-treated transparent plastic films to a
thickness of about 50 microns. The coating is then
magnetized and photopolymerized into a pressure-sensitive
adhesive state. The resulting sheet can be cut into strips.


1 3398 1 0
-65-



Example 20 - Preparation of an Electrically Conductive
Adhesive Material Containing Silver-Coated Aluminum
Particles



An electrically conductive adhesive material containing
5 silver-coated aluminum particles is prepared by mixing from
73 - 80 parts by weight of a silver-coated copper-seeded
aluminum powder prepared according to the process of Example
3, above, with about 20 parts by weight of a solid polyamide
resin, such as is commercially available under the name of

*




10 VERSALON 1100, 5 parts by weight of a liquid polyamide
resin, such as is commercially available under the name
VERSAMID 125, 24 parts by weight of toluene, and 26 parts by
weight of ethanol.




Example 21 - Preparation of an Electrically Conductive
15 Adhesive Paint Containing Silver-Coated Nickel Particles



An electrically conductive adhesive paint containing
silver-coated nickel powder particles is prepared by
combining 3 parts by weight of the copolymer base mixture
prepared according to Example 17, above, with 4 parts by
20 weight of trichloroethylene. The ingredients are heated and
stirred until a clear solution forms. To this clear liquid
solution is then added 12 parts by weight of silver-coated
nickel powder particles prepared according to the process of
*Trademark

' -66- 1 33981 0

Example 2, above. lhe highly volatile trichloroethylene is
then allowed to evaporate, leaving a thin film of
electrically conductive pressure-sensitive material.




Example 22 - Preparation of an Electrically Conductive
5 Adhesive Paint Containing Gold-Coated Nickel Particles



An electrically conductive adhesive paint containing
gold-coated nickel powder particles is prepared in the same
manner as is described in Example 21, above, except that
gold-coated nickel powder particles, prepared according to
10 the process of Example 4, above, are substituted for the
silver-coated nickel powder particles.




Example 23 - Preparation of an Electrically Conductive Ink
Containing Silver-Coated Nickel Particles



A polyester-based electrically conductive ink containing
15 silver-coated nickel particles is prepared by mixing 16.78

parts by weight of silver-coated nickel powder particles
prepared according to the process of Example 2, above, with
100 parts by weight of a polyester resin solution containing
about 35 weight percent solids, and about 0.5 parts by
20 weight of a flow modifier, such as MODAFLOW, as is available
from Monsanto Corp., St. Louis, Missouri.


*Trademark

-67- 1}39810

The foregoing examples are representative of the range
of coated products which can be prepared according to the
process of this invention and are not intended to be in any
way limiting. Application of the process of this invention
to the preparation of other coated products within the scope
of the claims which here follow will be readily apparent 'to
those skilled in the art.


Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Administrative Status , Maintenance Fee  and Payment History  should be consulted.

Administrative Status

Title Date
Forecasted Issue Date 1998-04-14
(22) Filed 1989-08-28
(45) Issued 1998-04-14
Deemed Expired 2003-04-14

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1989-08-28
Maintenance Fee - Patent - Old Act 2 2000-04-14 $50.00 2000-03-31
Maintenance Fee - Patent - Old Act 3 2001-04-17 $50.00 2001-04-12
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
OSTOLSKI, MARIAN J.
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Representative Drawing 2001-12-11 1 12
Drawings 1998-04-14 3 51
Description 1998-04-14 67 2,231
Claims 1998-04-14 54 2,684
Cover Page 1998-04-23 1 19
Abstract 1998-04-14 1 24
Fees 2001-04-12 1 28
Fees 2000-03-31 1 29
Prosecution Correspondence 1997-11-03 3 76
Prosecution Correspondence 1997-09-26 2 77
Prosecution Correspondence 1997-09-19 1 49
Prosecution Correspondence 1992-11-06 7 294
Examiner Requisition 1992-07-09 1 73
Office Letter 1998-03-10 1 55
Office Letter 1997-10-30 1 44
Office Letter 1989-01-22 1 33