Zinc alloy plating, not
including brass, didnt receive any meaningful recogni- tion
until the early 1980s. Since then, the range of zinc alloys has increased
and the production processes have been refined considerably. However,
it was within the last five to ten years that these processes gained
any commercial acceptance. This delay was the result of several factors:
- No compelling need had developed for the advantages offered
by the alloy deposits.
- The processes were difficult to operate consistently.
- The cost of operating the alloy baths was too high.
- There was no general consensus as to which alloy was the most
suited and cost effective for any particular application.
These factors were overcome by two developments in the automotive
and electronics industries. The first was the push for an environmentally
acceptable method to obtain increased corrosion protection. The
second was the pursuit of an acceptable replacement for cadmium
deposits. The zinc alloy baths available today are capable of satisfying
both of these needs. The deposits from zinc alloy baths are capable
of not only providing enhanced corrosion protection but also increased
lubricity, ductility and hardness.
Commercially
Available Zinc Alloy Processes
There are a number of commercially available zinc alloy processes,
including zinc/nickel (Zn/Ni), zinc/nickel/iron (Zn/Ni/Fe) zinc/cobalt
(Zn/Co), zinc/cobalt/iron (Zn/Co/Fe), zinc/iron (Zn/Fe), tin/zinc
(Sn/Zn) and zinc/manganese (Zn/Mn). Of these processes, the nickel,
cobalt and iron alloys are the only ones of any real commercial
concern. The plating processes for the iron, cobalt and nickel alloys
are operated and have additive systems similar to their non-alloy
counterparts (see Table I). The zinc/manganese
alloy is only of interest where galvanic compatibility with magnesium
is required. The tin/zinc alloy deposit usually contains a maximum
of about 30% zinc, has properties closer to those of tin and is
deposited from baths with no real similarity to normal zinc plating
baths or those used for other zinc alloys.
| Table
I - Zinc Alloy Processes |
| Alloy
Type |
Alloy
Composition |
Plating
Processes |
| Zn/Ni
Zn/Ni
Zn/Co
Zn/Fe |
5-10%
nickel (low)
10-15% nickel (high)
0.2-1.2%
0.2-1.2% |
Alkaline
non-cyanide or acid chloride
Alkaline non-cyanide or acid chloride
Alkaline non-cyanide or acid chloride
Alkaline non-cyanide |
Zinc/Nickel. The operating parameters for the alkaline
and chloride Zn/Ni systems are shown in Table II. In general, the
zinc/nickel alloy, whether alkaline or chloride, is by far the most
expensive to operate of any of the alloys discussed here. But, it
does have some advantages that the other alloys dont have.
It provides the best corrosion protection, maintains a majority
of its corrosion protection even at elevated temperatures and provides
greater wear resistance.
The alkaline plating process gives good plate distribution but
has very low efficiency and the complexers that are used can adversely
affect waste treatment. It is because of these complexers that a
zinc/nickel/iron trialloy is usually plated. This codeposition of
iron seems to have no affect on the performance of the deposit.
The zinc and nickel are replenished using either zinc anodes or
a galvanic zinc generator and nickel salts. If a generator is used,
the anodes are nickel, but nickel salts are still required.
Chloride plating systems, unlike the alkaline ones, will easily
plate hardened and cast metal parts and operate at almost 100% efficiency.
However, the alloy and plate distribution of chloride systems is
not as uniform as those of alkaline systems. In most chloride baths,
the zinc and nickel are replenished using nickel salts and zinc
anodes. An alternate, though less popular, approach is to use zinc
and nickel anodes on separate rectifiers.
| Table II - Zn/Ni Operating
Parameters |
| |
Alkaline
Zn/Ni or Zn/Ni/Fe |
Chloride
Zn/Ni Potassium |
Chloride
Zn/Ni Ammonium |
| Zinc (oz/gal) |
0.8-2.3 |
3.5-8.0 |
25.-6.0 |
| Nickel
(oz/gal) |
0.1-0.3 |
3.0-6.5 |
2.5-5.0 |
| Sodium
or Potassium Hydroxide (oz/gal) |
15-25 |
|
|
| Ammonium
Chloride (oz/gal) |
|
|
30-40 |
| Potassium
Chloride (oz/gal) |
|
|
25-33 |
| Proprietary
Additives |
As recommended
|
As recommended |
As recommended |
| pH |
|
5.0-6.0 |
5.5-6.0 |
| Temperature
(F) |
70-95 |
80-125 |
85-110 |
| Agitation |
Yes |
Yes |
Yes |
| Filtration |
Yes |
Yes |
Yes |
| Type of
Operation |
Rack or
barrel |
Rack or
barrel |
Rack or
barrel |
| Anodes |
Nickel
or zinc |
Zinc or
zinc and nickel |
Zinc or
zinc and nickel |
| Voltage
(v) |
2-13 |
2-12 |
2-12 |
| Current
Density (asf) |
1-30 |
5-25 |
5-25 |
| Plating
Efficiency (%) |
40-70 |
95-100 |
95-100 |
| Alloy
Composition (% Ni) |
5-15 |
6-15 |
6-15 |
| Alloy
Distribution |
Good |
Fair |
Fair |
| Plate
Distribution |
Good to
excellent |
Fair |
Fair |
Zinc/Iron. Unlike the cobalt and nickel alloys, the iron
alloy can only be produced using an alkaline non-cyanide process
(see Table III). But, it is the most economical and easiest of the
zinc alloy systems to operate. The deposit has very good corrosion
resistance, ductility and weldability. The iron alloy has only one
real negative it loses a fair amount of its enhanced corrosion
protection when exposed to elevated temperatures. It is for this
reason that it is not recommended for applications where it will
experience temperatures greater than 200F.
| Table
III - Zn/Fe Operating Parameters |
Zinc
(oz/gal)
Iron (ppm)
Sodium or potassium hydroxide (oz/gal)
Complexer (oz/gal)
Proprietary additives
Temperature (F)
Agitation
Filtration
Type of Operation
Anodes
Voltage (v)
Current Efficiency (asf)
Plating Efficiency (%)
Alloy Composition (% Fe)
Alloy Distribution
Plate Distribution |
1-3
30-120
16-28
1-4
As recommended
70-95
Yes
Yes
Rack or barrel
Zinc or steel
1-15
2-50
60-90
0.2-1.0
Good
Excellent |
Zinc/Cobalt. Alkaline systems for plating zinc/cobalt
alloys are easy and economical to operate and produce a deposit
with exceptional alloy and thickness uniformity (see Table IV).
Like the alkaline nickel alloy process it is not unusual to actually
plate a trialloy of zinc/cobalt/iron because of the presence of
complexers. The alkaline plating process is preferred but the chloride
system can be used where it is necessary to plate hardened or cast
metal parts.
Choosing
the Right Zinc Alloy Process
There are only two choices to be made. The first is the type of
alloy that is required. The second, in the case of nickel and cobalt
alloys, is whether to use an alkaline or chloride plating bath.
The first choice is easy, since this is usually spelled out in the
customers specifications. The choice of bath types can be
a little more involved. There are several considerations that need
to be taken into account:
- SubstrateSome
substrates, such as cast iron, hardened or carbonitrided parts,
require chloride type baths to plate correctly.
- EquipmentThe
chloride baths necessitate the use of corrosion-resistant equipment.
All of the alkaline alloy baths contain complexers of one kind
or another that can also be corrosive to equipment. Depending
on the alloy bath and the complexers used, it may be necessary
to use more corrosion resistant equipment than would be required
for a normal alkaline zinc plating bath.
- Waste TreatmentIn
the case of nickel alloys, it will be necessary to determine what
if any modifications will be necessary to handle the nickel in
the effluent. Since the alkaline baths contain complexers, the
effect of these materials on the ability to remove metals from
the waste stream will need to be addressed as well.
| Table IV - Zn/Co Operating
Parameters |
| |
Alkaline
Zn/Co or Zn/Co/Fe |
Chloride
Zn/Co Potassium |
Chloride
Zn/Co Ammonium |
| Zinc (oz/gal) |
1-3 |
3.5 |
2.5-4.5 |
| Cobalt |
30-120
ppm |
0.2-0.6
oz/gal |
0.2-0.6
oz/gal |
| Sodium
or Potassium Hydroxide (oz/gal) |
16-28 |
|
|
| Ammonium
Chloride (oz/gal) |
|
|
4-8 |
| Potassium
Chloride (oz/gal) |
|
25-35 |
15-20 |
| Boric
Acid |
|
2.5 |
|
| Complexer
(oz/gal) |
1-4 |
|
|
| Proprietary
Additives |
As Recommended |
As Recommended |
As Recommended |
| pH |
|
4.7-5.2 |
5.0-6.0 |
| Temperature
(F) |
70-95 |
75-110 |
75-110 |
| Agitation |
Yes |
Yes |
Yes |
| Filtration |
Yes |
Yes |
Yes |
| Type of
Operation |
Rack or
barrel |
Rack or
barrel |
Rack or
barrel |
| Anodes |
zinc or steel |
Zinc |
Zinc |
| Voltage
(v) |
1-15 |
2-15 |
2-15 |
| Current
Density (asf) |
2-50 |
1-35 |
1-35 |
| Plating
Efficiency (%) |
60-90 |
95-100 |
95-100 |
| Alloy
Composition (% Ni) |
0.2-1.0 |
0.2-1.0 |
0.2-1.0 |
| Alloy
Distribution |
Good |
Fair |
Fair |
| Plate
Distribution |
Excellent |
Fair |
Fair |
Because of the alloy content of the deposit, special chromate formulations
are required for each of the different alloy deposits. Without a
chromate conversion coating the corrosion characteristics of the
iron and cobalt alloys are not significantly different than those
of pure zinc. In the case of nickel alloys, with no chromate, the
onset of white salt corrosion is about the same as for pure zinc
but the progression of the corrosion is slowed depending on the
nickel content.
The only passivation process that is of current commercial interest
for the iron alloy is a non-silver black chromate. A yellow chromate
is available but is not in much demand. There presently is no clear
chromate for the iron alloy since the iron tends to discolor chromate
films. Iron alloys seem to attain their increased corrosion protection
from a change in the physical characteristics of the chromate conversion
coating.
There are clear, yellow and black chromate conversion coatings
available for the nickel alloys. The improved corrosion protection
of the nickel alloy appears to be achieved by shifting the corrosion
potential of the deposit closer to that of the steel substrate while
still maintaining its sacrificial nature.
There are clear, yellow and black chromate conversion coatings
available for the cobalt alloys. The cobalt alloys appear to obtain
their increased corrosion protection from a modification of the
physical properties of the chromate conversion coatings.
The yellow chromate over an alloy deposit is darker and more highly
iridescent. This modified yellow is not only accepted in the industry,
but is used by some as a method of differentiating alloy from non-alloy
zinc. When processed properly, the clear chromates on the cobalt
and nickel alloys and black chromates on the iron, cobalt and nickel
alloys look very similar to the chromate coating on non-alloy zinc
deposits.
In addition to the chromate conversion coatings, topcoats are also
used to improve corrosion protection and lubricity and to reduce
the loss of corrosion protection at elevated temperatures.