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ELECTROLESS PLATING
CHAPTER 21
ELECTROLESS PIATING
The electroless plating process, also called
autocatalytic deposition, deposits a uniform coat-
ing onto catalytic surfaces, regardless of the shape
of the part. Once a primary layer of metal has
formed on the substrate, that layer, as well as each
subsequent layer, becomes the catalyst that causes
the reaction to continue. Electroless plating, in
contrast to conventional plating, does not use
external electric current to produce a deposit.
Deposition occurs in an aqueous solution contain-
ing metal ions, a reducing agent, and a catalyst
(part). Chemical reactions on the surface of the
catalytic part being plated cause deposition of the
metal or alloy. Table 21- I lists the different com-
ponents in the plating solution, along with their
respective functions.
Nickel is the most common metal deposited
autocatalytically. The chemical reactions that occur
when using sodium hypophosphite as the reducing
agent are as follows:
(HZP02)- + H20 + (HZP03)- + H2
Both nickel and phosphorus are reduced simul-
taneously, and the coatings produced are metastable
solutions of phosphorus in nickel. When the
coatings are properly heat treated, nickel-phosphide
particles, which increase hardness and improve
wear resistance, form within the coating. The
coating thickness is not limited, except by practical
considerations.
Electroless
CHAPTER
CONTENTS:
Metals
Deposited
21-1
Plating
Process
21-3
Precleaning
21-3
Cleaning
21-4
plating provides several unique
Initiating
21-4
Plating
21-4
characteristics
superior
to electrode position
processes:
Process
Control
21-4
l
The process produces a uniformly thick
coating on both simple and complexly
shaped workplaces.
The process may be applicable to a variety of
substrates ranging from metals and semi-
conductors to nonconductors.
The use of an auxiliary power supply and the
need for electrical contact is eliminated,
except for precleaning and surface activa-
tion purposes.
Some electroless deposits have unique and
controlled chemical, mechanical, and mag-
netic properties.
Deposit
Properties
21-9
l
Equipment
21-9
Appearance
and Adhesion
21-9
l
Porosity
21-10
(1)
Hardneas
21-10
catalyst
Ni++ + H2P020 + H20 -
NiO + (H2P03)- + 2H+
Thickness
21-10
(2)
l
Composition
21-11
(HjPOz)- + H+ - P + OH-+ H20
(3)
Corrosion
Resistance
21-11
METALS DEPOSITED
Wear
Resistance
21-11
Safaty and
Environment
21-11
Electroless plating processes are used by indus-
try to alter the surface of a part, providing a
uniform, conductive metallic coating. Nickel,
copper, cobalt, and gold are the most commonly
deposited metals. The commercially produced
electroless alloys are listed in Table 21-2.
Composite coatings have also been successfully
deposited. These coatings consist of particles of
such materials as synthetic diamonds, silicon car-
bide, aluminum oxide, and polytetrafluorethy lene
(PTFE), codeposited with nickel or cobalt. Com-
posite coatings enhance the wear and friction
characteristics of the metal deposit.
Producing specific properties in the deposit
from a particular plating process requires careful
control. For example, the hardness of the base
metal determines which heat treatments are
required to prevent hydrogen embrittlcmcnt caused
by the pretreatment processes. It maybe necessary
to control the surface finish, elongation, structure
of the deposit, reflectivity, conductivity, melting
point, composition, coefficient of thermal expan-
sion, density, internal stress, and elasticity to
achieve specified properties. The producer must
therefore have a working knowledge of how the
process parameters affect the deposit, Some of the
properties of electroless metal deposits are sum-
marized in Table 21-3.
PROPERTIES
The properties of electroless coatings are varied
and are determined by the specific metal and
process employed. In the case of electroless nickel,
the corrosion and wear resistance, conductivity,
solderability,
and magnetic
properties
of the
APPLICATIONS
The applications of electroless metal deposits
are many and diverse. Each metal has specific applica-
tions for which it can be used. Typical metal deposits
include copper, gold, nickel, and nickel alloys.
deposit find useful application.
Contributors of sections of this chepter are: Dr. George D. DiBari, Product Manager, Technical Services,
International Nickel, Inc.; Phil Stapleton, Technical Director, Stapleton Company & Associates.
Reviawers of sections of this chapter are: Teri L. Arney, Senior Rasearch Chemist, Elnic, Inc.; Edward G.
Buckley, Technical Service Manager, Technic, Inc.; Barry R. Chubs, Technical Marketing Specialist, Enthone,
Inc.; Dr. George D. DiBari, Product Manager, Technical Services, International Nickel, Inc.; Ronald Duncan,
Director of Research and Engineering, Ehric, Inc.; Dr. Nathan Faldstein, Surface Technology, Inc.; Gerald A.
Laitinen, Product Manager. Allied Kelite Products,
Witco Chemical Corp.; Jovona L. McDowell. Manager.
Laboratory Services, Elnic, Inc.; Gary Sha whan, Electroless
Nickel Product Managar,
Enthone,
Inc.; Phil
Stapleton,
Technical Director,
Stapleton Company & Associates.
21-1
Tool and Manufacturing Engineers Handbook Knowledge Base •
Copyright © 1998 •
Society of Manufacturing Engineers
CHAPTER 21
METALS DEPOSITED
Copper
Electroless copper deposits are used in engineering applica-
tions to provide conductivity, such as in the through-hole
plating of printed circuit boards and in the preparation of
plastics for decorative plating. The deposits are uniform,
conductive, and can be applied over many substrates that have
been properly activated. Electroless copper deposits are also
being
used, in combination with electroless nickel, to solve
electromagnetic shielding problems.
Gold
Electroless gold deposits are used for improving solder shelf
life by preventing oxidation of the surfaces. Gold deposits are
normally thin, under 0.1 mil (1 mil = 0.001”) (2.5 ~m), and are
applied over electroless nickel, which prevents diffusion of the
gold into copper. Electroless gold is used in electronic applica-
TABLE 21-2
Commercially Produced Electroless Alloys
TABLE 21-1
Typical Components in Electroless Plating Solutions
Electroless
Process
Au
b
Ni Co P
B T1 Trace
Copper
99.9
0.1
Component
Function
Gold
99.98
0.02
Metal salt
Provide the metal ions to be
Nickel
phosphorus low
(e.g., nickel sulfate)
plated.
98
2
0.3
Reducing agent
Provide the reducing power at
Nickel
phosphorus
medium
(e.g., sodium
the catalytic interface.
hypophosphite)
94
6
0,3
Completing
agent
Completing of the metal ions
Nickel
phosphorus high
(chelators)
and preventing bulk
89
11
0.1
decomposition.
(e.g., lactic acid)
Nickel cobalt
phosphorus
Buffering agent
To resist the pH changes
75
20 5
0.3
(e.g., acetic acid)
caused by the hydrogen
released during deposition.
Nickel cobalt
phosphorus
Accelerators (Exultants)
To help increase the speed of
the reaction.
16 78 6
0.3
Nickel boron
99.5
0.5
0.1
Inhibitors (Stabilizers)
To control reduction reaction
in the plating solution.
Nickel thallium
boron
92
3.5 4.5
0.3
(Stapleton
Company)
TABLE 21-3
Summary of Deposit Properties
Property
Cu
Au
NiP9
NiCoP
NiB
NiTIB
Hardness,* Vickers
(100 g load)
---
---
500-550
570
650-700
750
Modulus of elasticity,
106 psi (GPa)
---
---
17-28.4
(118-196)
---
( ::8)
(f’:8)
Tensile strength,
ksi (M Pa)
---
---
35.5-128
(245-883)
42.7-99.5
---
15.6
(108)
(294-686)
---
Internal stress,
ksi (M Pa)
Density, g/ cm3
---
___
-4.3 to +42.7
(-29 to +294)
+42.7
(+294)
+15.6
(+108)
8.9
19.3
7.95
8.1
8.3
8.25
Thermal expansion,
pm/m” °C
16
14
13
13
10
12.1
Melting point,
OF~C)
1980
1940
1635
1740
2640
1980
1080)
(1060)
(890)
(950)
(1450)
(1080)
Magnetic, oersteads
o
0
1
up to
400
>5
>5
Resistivity, K Q” cm
1.6
2.1
20-110
20-110
<lo
30-70
(Stapleton Company)
*
Hardness values given are before heat treatment.
21-2
Tool and Manufacturing Engineers Handbook Knowledge Base •
Copyright © 1998 •
Society of Manufacturing Engineers
CHAPTER 21
METALS DEPOSITED
tions to provide coverage on isolated circuits where conventional
electroplating is not possible. Electroless gold deposits are also
being used on printed circuit boards to improve wear.
about 0.5-5 .0% boron, the balance being nickel. When they
contain between 3 and
4%
boron, these deposits possess good
wear and erosion characteristics for engineering applications.
Nickel Phosphorus
Electroless nickel-phosphorus deposits are widely used to
reduce corrosion and wear. Corrosion protection is provided by
isolating the base material from the environment and by the
natural oxide layers that form on the coating surface, Wear
resistance is provided bythenatural lubricity and hardness of
the coating. Electroless nickel can be deposited onto many
materials in thicknesses ranging from 0.05 to 100 roils (0.0013 to
2.5 mm). A typical engineering coating would be approximately
1 mil (25 ~m) thick. The amount of phosphorus is from 1 to 13%
and can generally be controlled to ~0.5Y0. The properties of
these coatings depend on the phosphorus content, which should
be specified when developing applications (see Table 21 4).
When electroless nickel deposits are heated to above their
transition temperature, 390-660° F (200-350° C), they begin to
precipitation harden and crystallize, Coatings have been pro-
duced that have harnesses greater than 950 Vickers using a
100 g load. During this process, the coating changes from an
amorphous structure to a mixture of nickel phosphide and
crystalline nickel. When mid-phosphorus deposits are heat
treated at 1380° F (750° C), they increase in strength; at the same
time, high-phosphorus deposits decrease in strength due to
greater shrinkage and the microcracking that may occur. Heat
treating high-phosphorus deposits at lower temperatures, 230-
400° F (1 10-200° C), and for a longer period of time helps to
increase hardness while minimizing microcracking.
Strength, elasticity, elongation, and ductility are improved
in deposits with high phosphorus, providing superior perform-
ance in many engineering applications including electrolcss-
formed bellows, hydraulic cylinders, and pressure vessels. Electro-
less nickel-phosphorus
Nickel Thallium Boron
Electroless nickel-thallium-boron deposits are used in high-
wear applications, providing excellent lubricity and high hard-
ness at high temperatures and high loads. Deposits containing
5T0thallium and 5% boron are applied over a wide range of base
materials in thicknesses of 0.5 to 2.0 roils (13 to 50 pm).
TABLE 21-4
Types of Electroless Nickel-Phosphorus Deposits
Deposit
Phosphorus
Type
Content, %
Comments
Low
1.5 2.5
These processes provide low-
phosphorus
temperature operations for
plating on plastics. The
coatings are high in stress and
produced from alkaline
solutions.
Medium
3.5 8.5
These processes provide
phosphorus
conventional electroless nickel
coatings. The deposits are
used for preventing wear and
corrosion in engineering
applications. Coatings may be
bright depending on the
chemistry, Solutions are
operated in a pH range of 4
to 5.
deposits are also being used to provide
High
9.3 13
These processes provide
electromagnetic
shielding for plastic cabinets and enclosures.
phosphorus
increased protection in
aggressive environments over
medium-phosphorus coatings.
The amount of trace metals
plated into the deposit are
reduced, producing a more
pure deposit. These processes
operate in a pH range of 4 to
5. Coatings have higher
elongation and strength than
medium-phosphorus coatings
in the as-plated condition.
(Stapleton Company)
Nickel Cobalt Phosphorus
Electroless nickel-cobalt coatings are used in magnetic
applications where uniform, thin deposits are required. These
coatings are in the thickness range of 0.003 to 0,02 roils (0.07 to
0.5 pm) and contain between 20 and 80~ cobalt, depending on
the application.
Nickel Boron
Electroless nickel-boron deposits are used in place of
electroless gold, providing good wire bonding and solderability.
These coatings are hard, uniform, and conductive and contain
ELECTROLESS
PLATING PROCESS
Electroless plating processes depend on chemical reduction
PRECLEANING
reactions to deposit uniform metallic coatings on parts, elimi-
Precleaning removes heavy soils and scales on the surface
nating the need for external current. The coating is uniform on
and exposes the bare base material. The precleaning can be
all wetted surfaces. Thickness is determined by the length of
accomplished
by wet or dry blasting, vapor decreasing,
time the article or part is kept immersed in the sohttion. The
mechanical cleaning, and descaling, among other methods. In
entire process involves several different steps as discussed in
almost all cases, the base material will not be clean enough after
this section.
precleaning to achieve adequate adhesion. The surface will still
21-3
Tool and Manufacturing Engineers Handbook Knowledge Base •
Copyright © 1998 •
Society of Manufacturing Engineers
CHAPTER 21
ELECTROLESS
PLATING PROCESS
have oxides and oils present. For additional information, refer
to the various cleaning methods discussed in Chapter 16,
“Mechanical and Abrasive Deburring and Finishing,” and
Chapter 18, ’’Cleaning,’’ ofthis volume.
may be used to initiate electroless deposition. Special heat
treatments may be required on aluminum, beryllium, titanium,
and other metals to obtain maximum adhesion.2
PLATING
When a properly prepared material is placed into the
electroless plating solution, the surface potential reaches a value
where metal deposition is possible. The deposition potential is
dependent on the pH, temperature,
CLEANING
Cleaning removes the oils and organic material on the
surface of the parts and is first accomplished by soaking in a
solubilizing solution at an elevated temperature. Some base
materials require electrocleaning as a second step to remove
carbon or grinding material. The last step is to completely
remove the oxides inan acidic solution.
The cleaning of metals prior to electroplating is discussed in
American Society for Testing and Materials (ASTM) Standard
B 322. Most of the information in that standard is applicable to
the preparation of metals for electroless deposition. Additional
information can be obtained in those standards that deal with
specific metals and alloys. 1
ionic concentration,
and
chemical composition of the solution.
As the potential changes, a charge between the solution and
the base material is created. The charge causes the cations in the
solution to organize themselves and produce what is called the
matrix. This matrix is like a blanket that covers the surface and
controls the deposition process. The reducing agents in the
solution provide electrons at the interface. Through several
sequential reactions within the matrix, the metal ions in
solution are reduced, producing the coating.
Each electroless plating process uses unique chemistry to
achieve this reduction reaction. Powerful reducing agents like
sodium borohydride and titanium trichloride are used to plate
out thallium and gold, while sodium hypophosphite and
formaldehyde will reduce nickel and copper, respectively. The
concentrations of these reducing agents and the metal salts
change as the plating process proceeds and by-products are
produced. To sustain the reduction reactions, additions of fresh
chemicals must be made. In addition, the special additives used
to provide brightness, stability, wetting, controlled cloud
points, and controlled transition temperatures must be moni-
tored and kept at optimum levels.
Proprietary electroless processes are available, and suppliers
of these processes provide instructions for maintaining and
controlling individual processes. Electroless processes can be
maintained by performing simple chemical analyses from which
chemicals required to replenish the solution can be determined.
INITIATING DEPOSITION
Autocatalytic nickel will usually deposit on clean, wetted
surfaces. Aluminum, beryllium, platinum metals, iron, cobalt,
nickel, titanium, and their alloys can be plated directly. Certain
base metals cannot be plated directly; these include zinc, lead,
cadmium, tin, bismuth, arsenic, antimony, and alloys containing
large proportions of these metals. The metals that cannot be plated
directly should be electroplated with a thin copper or nickel
strike prior to being immersed in the electroless plating sohrtion.
Preliminary electrolysis or contact with a catalytic metal like
iron or nickel is required for deposition on copper, silver, gold,
carbon, vanadium, molybdenum, tungsten, chromium, selenium,
and uranium. In some cases, immersion deposition processes
CONTROLLING THE PLATING PROCESS
Impurities in the solution can affect the ductility, corrosion
resistance, and appearance of electroless deposits while con-
taminants in the solution can cause pitting, adhesion, and
roughness problems. Hence, the solution must be kept relatively
free of impurities to control the properties of the deposit and
avoid producing defectively coated parts that must be scrapped
or reprocessed at great expense to the metal finisher.
A deliberate, sustained campaign to keep impurities out of
solution is better than having to resort to time-consuming and
expensive treatments to remove contaminants. For this effort to
be successful, everyone involved in processing the parts should
become familiar with the sources of impurities, which are one or
l
Defective exhaust ducts.
l
Tank Ieachates and defective rack coatings.
. Grease and oil from pumps, hoists, and overhead
equipment.
. Dissolution of metals or parts that accidentally fall into
the solution.
l
Hard water (calcium sulfate).
Assuming that all potential sources of contamination can be
identified, it should be possible to compile a list of actions to
maintain the purity of the solution and, consequently, avoid
generating rejects. Some recommended actions are as follows:
more of the following:
l
Remove metals or parts that have fallen into the solution
as quickly as possible.
Use adequate rinses and electrocleaning
. Contamination from alkaline cleaners, acid pickling
solutions, and other solutions by direct transfer (drag-in),
l
in the prepa-
or by airborne spray.
l
Airborne particulate matter; for example, from grinding
ration process.
Monitor the conductivity of rinse tanks to check cleanli-
ness of the water and monitor excessive drag-out levels.
Exhaust grinding and polishing equipment properly, or
isolate these processes from the plating area.
Use de-misting agents to prevent airborne spray.
l
and polishing operations.
l
Improper removal of grease, oil, and buffing and polish-
l
ing compounds from the work.
. Defective filters, pumps, and other equipment.
l
21-4
Tool and Manufacturing Engineers Handbook Knowledge Base •
Copyright © 1998 •
Society of Manufacturing Engineers
CHAPTER 2
CONTROLLING
THE PLATING PROCESS
. Inspect and maintain filters, pumps, and other auxiliary
l
Follow the instructions of the supplier of the process for
equipment on a regular schedule.
batb makeup, replenishment, and operation.
. Inspect and repair racks and rack coatings,
Despite all precautions, problems may occur. Table 21-5 lists
l
Maintain solution at near optimum levels, maintain
common problems that occur in electroless nickel plating, gives
temperature, and check pH on a regular basis.
the possible causes, and suggests solutions to these problems.~
TABLE 21-5
Troubleshooting Electroless Nickel Deposits3
Problem
Possible Causes
Suggested Solutions
Skip plating,
Improper cleaning.
Temperature should be checked as well as purity
and concentration of cleaner and other
pretreatment solutions.
poor coverage,
edge pullback
and frosted
edges
Improper activating,
Activators should be checked. Some metals and
alloys, such as leaded steels, brasses, copper,
aluminum and magnesium, require special
preparation.
Improper rinsing.
Rinse temperature and rinsing time should be
checked. Too long a time in a rinse may cause an
oxide film to form; too short a time may not
remove residual films. Rinses must be kept clean.
Metallic
contamination.
Bath should be dummied or discarded and
replaced.
Organic
contamination.
Bath should be cooled, carbon treated, and
filtered. Rinses should be checked for residual
drag-in.
Too much air agitation.
Air agitation should be reduced.
Roughness in
deposit
Contamination from
solid particles; i.e.,
dust, loose nickel, or
metal chips.
Turbidity of solution.
Solution should be filtered through #5 micro
filter at high flow rates.
May be result of high pH, which aids in
formation of metallic hydroxides. pH should be
checked and adjusted. Completers may be added.
Heavy or too rapid EN
solution replenishment
while work is being
plated.
Replenisher should be added slowly and mixed
thoroughly. Additions should be made in area as
far away from work as possible.
Contaminated
makeup
Quality of water should be checked. Water may
require carbon treatment and filtration.
Air agitation should be checked or temperature
adjusted. Derated heaters should be used.
Cleaning and rinsing should be improved.
water.
Localized overheating.
Particles of metal or
soil on work.
Contaminated filter
cartridges, liners, or
bags.
Liners should be leached prior to makeup. Filters
should be changed.
Only one side of work
affected.
Agitation around work should be increased.
Work rod or solution agitation should be
provided.
(continued)
21-5
Tool and Manufacturing Engineers Handbook Knowledge Base •
Copyright © 1998 •
Society of Manufacturing Engineers
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