CLZ
- 219 (BORIC ACID FREE) Economical chloride zinc process |
CLZ-219
is an economical two-component brightener system for use
in either mixed potassium/ammonium chloride or mixed sodium/ammonium
chloride zinc plating operations. CLZ-219 has excellent
leveling and covering power and will plate directly on carbo-nitrided,
carburized, or case-hardened steel and cast and malleable
iron. READ ENTIRE TECHNICAL DATA SHEET BEFORE USING THIS
PRODUCT.
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FEATURES/BENEFITS: |
- High mileage brightener.
- Value pricing .
- Outstanding brightness.
- Tolerant to contamination.
- Boric acid free.
- Very good covering power.
- Broad operating ranges.
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- Low cost of operation.
- Low cost of operation
- Maximum aesthetic impact
- Process reliability under
adverse conditions
- Elimination of anode polarization
caused by impure boric acid; No boron in effluent
- Deposits zinc over a broad
current density range
- Reliable and easy to control
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MATERIALS
REQUIRED |
CLZ-219
A is used for make-up and replenishment.
CLZ-219 B is used for make-up and replenishment.
CZ 515 A may be used in place of zinc chloride to make-up and
replenish zinc metal.
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EQUIPMENT
REQUIRED |
Tanks |
Plating
tanks of steel, lined with PVC, Koroseal, polypropylene
or Polyethylene are recommended. Rubber lined tanks are
not recommended. If they are to be used, a sample of the
tank liner should be submitted to your technical representative
for evaluation. Fiberglass tanks or tank liners may be
used. Before making up ZINCOBRITE CLZ-219 zinc solution
the tank must be cleaned and rinsed thoroughly. (CAUTION:
If changing from a cyanide zinc process, introduction
of acid may liberate cyanide gas.)
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Heating
and Cooling |
If
heating and/or cooling is desired, coils should be made
of Teflon or Titanium isolated from the direct current
circuit. Quartz immersion heaters may also be used. Cooling
coils should be made of Teflon or titanium isolated from
the direct current circuit.
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Filtration |
Barrel
plating installations require continuous filtration to
remove iron sludge contamination from the plating solution.
The filtration system should have sufficient capacity
to filter the plating solution two times per hour. All
filter parts that come in contact with the plating solution
should be nonmetallic. Do not use cellulose in any form
as a filtering medium; Dyne or diatomaceous earth is recommended.
Leached filter cartridges may also be used (15 microns).Periodic
use of a light carbon pack on the filter is recommended
(at least once per month). Use activated Carbon.
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Anodes |
Flattop,
ball, oval or slab anodes may be used. Anodes
should be pure zinc, ASTM Standard Specification B6
Special High Grade (99.99%).
Baskets made of pure titanium may be used with appropriate
pure zinc anode metal if the applied voltage does not
exceed 9 volts. Baskets must be kept full, with all the
zinc below the level of the solution. Baskets and anodes
should be kept clean to maintain good contact between
the basket and the zinc anode metal. Anode area must be
sufficient to keep anode current density
below 30 ASF (3.0 ASD). Do not use steel anode baskets
or steel anode hooks.
If roughness is noted, in most cases, anodes should be
bagged as a primary step in eliminating the difficulty.
Anode bags must be Dynel or polypropylene. Anode bags
should also be cleaned periodically. Roughness may also
be due to incorrect anode current density, or high pH
or burning.
Cover bus bars to minimize corrosion and possible solution
contamination. Bus bars must be elevated and not submerged
in the solution. Bus bars can be nickel plated to resist
corrosion.
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Power
Source |
A
12-volt power source is required for barrel plating. Rectifiers
must have low ripple (5% maximum). Ensure that the current
for the plating tank is measured with a reliable meter.
Stray alternating currents, current interruptions, and
excessive ripple in the power source must be avoided.
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OPERATING
CONDITIONS |
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Range
|
Zinc
Metal |
22-37
gm/l |
Potassium
Chloride |
130-190
gm/l |
Ammonium
Chloride |
30-60
gm/l |
Total
Chloride |
120-150
gm/l |
CLZ
: 219 A |
30-40
ml/l |
CLZ
: 219 B |
0.6-0.8
ml/l |
Replenishment |
Determined
by plating cell test |
pH(electrometric) |
5.0-5.5 |
Temperature |
21-41º
C(Optimum-27º C) |
Agitation |
Air
agitation is recommended |
Filtration |
Continuous |
Anodes |
Pure
Zinc(99% zinc) |
Anode
to Cathode Ratio |
2:1
minimum |
Anode
Current Density |
10-30
amp/sq. ft |
Cathode
Current Density |
1-25
amp/sq. ft |
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MAKE-UP
PROCEDURE : |
Prior
to making up CLZ-219 zinc plating solution, the processing
tank must be cleaned and rinsed thoroughly. In addition, the
tank should be leached for a minimum of 24 hours. (See Leaching).
- Add 50 litres of warm water, 54
°C to the 100 litres tank.
-
Add 8 litres of CZ 515 A with stirring.
-
Add 4.5 kg's. of ammonium chloride.
- Add
18 kg's. of potassium chloride and stir until almost dissolved.
-
Check the pH of the solution with a pH meter. Adjust if
necessary to 5.0 to 5.5
With technical grade hydrochloric acid to lower the pH or
potassium hydroxide to raise the pH.
-
Add 3-4 litres of CLZ: 219 A and 50 ml of CLZ: 219 B with
stirring.
-
Add sufficient water to bring solution to final operating
volume.
-
Recheck pH and adjust if necessary. The plating solution
is now ready for
Production use.
Production use.
1
Liter |
Ammonium
chloride |
45 |
grams |
Potassium
chloride |
180
|
grams |
ZINCOBRITE
CLZ LIQUID |
60
|
ml
|
ZINCOBRITE
CLZ-912A |
30-40
|
ml |
ZINCOBRITE
CLZ-912B |
0.60-0.80
|
ml
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Water
to make |
1
|
litre
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OPERATION
: |
Potassium
Chloride/Ammonium Chloride
Potassium chloride or ammonium chloride used in making up
and replenishing CLZ : 219 solutions must not contain humectants
such as tricalcium phosphate, or
any organic additives. Use only chemical grade potassium chloride
or ammonium chloride.
Rinsing
Rinsing after plating in CLZ :219 must be thorough and the
last rinse tank should be clear at all times. After removal
from the plating solution, allow the solution to drain from
the parts above the plating tank or in are covery tank before
water rinsing to reduce drag-out losses, thereby reducing
operating cost.
Maintenance
Analyses the solution frequently so that it remains in chemical
balance and will not require a large addition of chemicals
at any one time to restore solution balance. Always analyze
and adjust the zinc and chloride contents before adding CLZ:
219 A and CLZ: 219 B After making a corrective addition of
potassium chloride and ammonium chloride in a 4:1 ratio by
weight, measure the pH and adjust to the operating range use
technical grade hydrochloric acid to lower the pH or with
potassium hydroxide to raise the pH.
CZ 515 A may be used to increase the zinc metal content of
the CLZ : 219 solution when the zinc metal content of the
solutions is depleted too quickly to be replaced by the anodes,
as in the case of excessive drag-out. In such cases, CLZ :
219 may be added to the operating solution to raise the zinc
metal content. and total chloride content of the solution
by 250 ml of CZ : 515 A added to 100 liters of operating solution
will raise both the zinc metal content and total chloride
content of the solution by 1 g/L).
The major factors that determine brightener consumption are
drag-in of rinse water, drag-out of plating solution, temperature,
and electrolysis. CLZ : 219 B consumption should range from
250 ml per 1000 Amp/ Hour. However, additions of CLZ : 129
B are best determined by plating cell test and visual observation
of the work. There may be a tendency to add an excessive amount
of CZ: 219 B to the plating solution based upon plating cell
tests made without agitation. Part of the brilliance of the
CLZ: 219 deposit obtained in production is due to agitation
of the solution. Therefore, it is advisable to agitate the
test cell solution during test plating.
Additions should be one part CLZ: 219 A for every 1 to 3 parts
of CLZ: 219 B replenished based on operating experience and
drag-out.
Agitation
Air agitation and solution circulation are highly recommended.
Air agitation will help remove iron from the plating solution
and reduce the need for hydrogen peroxide. Solution circulation
may be achieved in large plating tanks in automatic lines
by placing the intake and discharge of the filtration system
at opposite ends of the tank, counter current to the workflow.
Low-pressure air (not compressed air) should be used and the
blower intake should be equipped with a filter to remove particles
to ensure that only clean air enters the solution. Do not
place the blower air intake in an area where it may pick up
acid fumes or other contaminants. The blower size formula
is: 1 cubic foot per minute for each foot of perforated agitation
pipe with blower pressure at 1 pound per square inch for each
18 inches of solution depth. Your local representative will
be pleased to make recommendations concerning equipment.
pH
Control
Maintain pH between 5.0 and 5.5 with frequent small additions
of diluted technical grade hydrochloric acid. Never use acid
that is green. When measuring pH use a meter.
Temperature
Optimum temperature is 27°C. Recommended operating temperature
range is 21 to 41 °C.The solution can be operated above
38° but brightener consumption will increase significantly;
however, deposits will be bright and level. The solution will
operate at lower temperatures and produce bright level deposits;
however, plating efficiency decreases at lower temperatures.
Impurities
The major contaminant in all chloride zinc plating solutions
is iron. This contamination is normally controlled in the
CLZ: 219 process by the use of air agitation along with solution
filtration. If hydrogen peroxide is to be used, contact your
local representative for the recommended procedure.
Leaching
The tank should be leached for 24 hours minimum as follows:
NOTE: If changing from a cyanide zinc process, introduction
of acid may liberate cyanide gas. Cyanide gas is poisonous.
Leaching should be done only with adequate exhaust ventilation.
It may be necessary to have the exhaust scrubbed. 1. 2. 3.
Prepare a leaching solution consisting of 3% by volume technical
grade hydrochloric
acid and 97% water. If possible, heat to 49°C to accelerate
the leaching process.
Add 75 ml of CLZ- 219 A for each 100 liters of leaching solution.
Fill
plating tank to the top of the tank and let solution stand
for 24 hours.
Drain tank and rinse thoroughly with water.
If
fiberglass tanks are used, leaching must be most thorough.
In addition, the tank or lining manufacturer should warrant
that no mold release was used in tank construction or specify
the mold release and methods of removing any impregnation
from the fiberglass.
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SAFETY
AND HANDLING INSTRUCTIONS |
DANGER!
CZ: 515 A AND THE CLZ: 219 OPERATING SOLUTION CONTAIN ZINC CHLORIDE,
WHICH CAN CAUSE SEVERE BURNS OF SKIN AND EYES. CZ: 219 B MAY
CAUSE BURNS TO EYES. CLZ: 219 A MAY CAUSE SKIN OR EYE IRRITATION.
HAZARDS: CZ: 515 A Liquid and the operating solution contain
zinc chloride which can cause severe irritation of respiratory
tract; severe burns to skin and eyes. Ingestion may cause toxic
effects. CZ: 219 B may cause severe irritation to respiratory
tract and skin, possible eye burns. CZ: 219 A can cause irritation
to skin and eyes. Do not get in eyes, on skin, or on clothing.
Do not take internally.
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CONSULT
SUPPLIERS MSDS FOR INFORMATION ON pH ADJUSTERS AND ADDITIVES
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FIRST
AID: In case of contact
of CLZ: 219 A, CLZ : 219 B, CZ 515 A LIQUID, pH adjusters,
additives or the operating solution; immediately flush skin
or eyes with plenty of water for at least 15minutes; for eyes
seek immediate medical attention. Remove and wash contaminated
clothing and shoes.
HANDLING
INFORMATION: When making up or adding to solutions,
always add CLZ: 219 A, CLZ: 219 B, CZ 515 A LIQUID, pH adjusters
and additives slowly and cautiously. Do not get in eyes, on
skin, or on clothing. Avoid breathing mist or vapors. When
handling CLZ : 219 A, CLZ : 219 B, CZ : 515 A LIQUID, pH adjusters,
additives or the operating solution wear chemical safety goggles,
face shield, rubber gloves, respirator, and protective clothing.
Avoid contamination with any other foreign material. Exhaust
ventilation is recommended to remove dust, mist or vapors
that may be generated during make-up and operation.
CONTAINER
INFORMATION: Keep containers tightly closed. Store
indoors in a cool, dry place. Loosen closure cautiously when
opening containers. Wash
Thoroughly after handling. Do not reuse containers, wash before
disposal. Improper disposal or reuse of containers may be
dangerous and illegal.
REFER TO MSDS FOR FURTHER SAFETY AND HANDLING INFORMATION.
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CONTROL |
The
following analytical procedures are recommended for use by
personnel who have been trained to use laboratory practices
which are considered safe and prudent by chemical industry
standards. Such practices include suitable personal protective
equipment, the use of proper equipment, the use of proper
methods of handling all chemicals and proper laboratory procedures.
Use only analytical reagent grade chemicals and deionized
or distilled water in the following analytical procedures.
CAUTION:
The following procedures involve the use of potentially hazardous
chemicals. Consult manufacturer's material safety data sheets
and follow the appropriate safety precautions.
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ANALYSIS
FOR ZINC METAL |
Equipment
Needed
2 ml pipette
25 ml graduated cylinder
50 ml burette
250 ml Erlenmeyer flask
Before
analysis treat the solution with activated carbon (2-3 Gms/Litre)
and filter.
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Zinc
|
Reagents
Required
- Ammonia
Ammonium chloride Buffer Solution
-
Eriochrome Black T Indicator
-
0.05 M E.D.T.A.
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Method |
Pipette
out 2 ml in a conical flask. Dilute with 25 ml distilled water.
Add 10 ml
Ammonia Ammonium Chloride Buffer Solution and a few drops of
Eriochrome
Black Indicator and titrate with 0.05 M E.D.T.A. to a blue end
point.
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Calculation |
1
ml 0.05 M E.D.T.A. = 0.003269 Gms Zinc
Burette reading X 1.635 =
Gms/Litre Zinc
Before analysis treat the
solution with activated carbon (2-3 Gms/Litre) and filter.
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Zinc
|
Reagents
Required
4. Ammonia Ammonium chloride Buffer Solution
5. Eriochrome Black T Indicator
6. 0.05 M E.D.T.A.
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Method |
Pipette
out 2 ml in a conical flask. Dilute with 25 ml distilled water.
Add 10 ml
Ammonia Ammonium Chloride Buffer Solution and a few drops of
Eriochrome
Black Indicator and titrate with 0.05 M E.D.T.A. to a blue end
point.
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Calculation |
1
ml 0.05 M E.D.T.A. = 0.003269 Gms Zinc
Burette
reading X 1.635 = Gms/Litre Zinc
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Total
Chloride |
Reagent
Required
1. Calcium Carbonate
2. Potassium Chromate Indicator
3. 0.1N Silver Nitrate
Pipette
out 2 ml solution in a 500 ml conical flask. Add 50 ml distilled
water and calcium carbonate in slightly excess to remove
free acidity. Add Potassium Chromate Indicator till solution
is distinctly yellow. Titrate with 0.1 N Silver Nitrate
till appearance of reddish
tinge on the precipitate.
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Calculation |
ml
of 0.1 N Silver Nitrate = 0.003546 Gms CL Burette
Reading x 1.773 = Gms/Ltr CL Total Chloride
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MATERIAL
SAFETY DATA SHEETS |
For
more detailed information on the toxicological properties of
the products described herein, reference can be made to the
Material Safety Data Sheet (MSDS) for each product. If you do
not have the proper MSDS, it can be requested from: YOUR LOCAL
representative.
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WARRANTY
AND DISCLAIMER |
The
information presented herein is to the best of our knowledge
true and accurate and all recommendations and suggestions appearing
in this bulletin covering the use of our products are based
upon information believed to be reliable. However, since the
conditions of use are beyond our control, this information is
given on the express condition and agreement that YOUR LOCAL
will not be liable to any person in contract, tort (including
negligence), and strict liability or otherwise for any claims,
damages or losses whatsoever. Nothing herein shall be deemed
a recommendation to use any product or process in violation
of any existing patent rights and no warranties, expressed or
implied, are made regarding the information, product, processes,
recommendations, description and safety notations contained
herein. The above includes proprietary information of YOUR LOCAL
representative and is furnished to you for your use solely on
products or processes supplied by us to you. |
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