- More uniform coverage by subsequent plating baths.
- Greater operating range for the double immersion surface conditioning treatment.
- Improved resistance to corrosion when followed by other deposits.
- 525 g/l NaOH
- 100 g/l ZnO
- 1 g/l FeCl3. 6 H2O
- 10 g/l KNaC4H4O6. 4H2O
Other modified immersion solution have employed copper and nickel together with the zinc. The proprietary Bondal process, involving a nickel containing solution such as describe in Leloup's patent, has received considerable commercial attentions, especially in Europe.
Dilute Zinc Immersion
Another variation has been developed for applications where rinsing and drag out are problems, as, for example, on automatic equipment. This variation consist of reducing the bath viscosity by lowering the concentration of the principle component. At the same time, a low coating weight must be maintained by a closer control of operating condition and by addition agents. Two typical dilute baths, which may be prepared in the usual manner, are as follows:
Chemicals Composition
NaOH ZnO KNaC4H4O6.4H2O FeCl3. 6 H2O NaNO3
Bath I, g/l 50 5 50 2 1
Bath II, g/l 120 20 50 2 1
Bath II will provide a greater zinc reserve for high production work with only a small sacrifice in rinsing and drag out properties. When using these dilute solutions the temperature must be maintained at 21 to 24oC and the immersion time must not exceed 30 sec.
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