Metal Finishing Guide Book

2013

Issue link: https://metalfinishing.epubxp.com/i/218436

Contents of this Issue

Navigation

Page 271 of 843

ability to oxidize Cr (III) to Cr (VI). Proper filming of the anodes is very important. New anodes should be dummied at plating current for several hours to develop the proper lead peroxide film. If the bath sits idle for several days it should be dummied again for 2–3 hours to reactivate the anodes. If the bath is to be idle for long periods of time it would be best to remove the anodes altogether. Some chrome platers will use rippled anodes, believing that such will give more surface area. As the anode works, however, the anode forms lead chromate in the groves of the ripple and the effective anode area is reduced. A smooth round anode is preferred to flat or rippled anodes. In addition to lead or lead alloy anodes there are specialized anodes that utilize platinized titanium as anodes. These are relatively expensive but allow for very precise chrome deposits. There are applications where the work is centered into a circular platinized titanium anode array and parts are plated to very close tolerances. In this case the cost is greatly justified as it eliminates post grinding operation and the need for excess chrome for grind stock. In the printing industry, for example, many companies utilize platinized titanium as gravure rolls are plated with chrome. Some very precise plating is done with platinized-titanium for I.D. plating of small ports on engines or other types of aircraft components. Some specialized equipment use platinized titanium for plating shock absorber rods. While it is not generally recommended, shops have successfully used steel wire to plate into I.D. ports or small diameter holes. These, however, eventually lead to rapid bath contamination. OPERATING CONDITIONS Typical operating conditions for functional or hard chrome are given in the following Table 1. Ordinary chemistry Mixed fluoride chemistry Mixed non-fluoride chemistry 120°F to 140°F 49°C to 60°C 130°F to140°F 54°C to 60°C 130°F to 150°F 54°C to 66°C Cathode Current Density 0.25 asi to 2.5 asi 4 asd to 38 asd 1asi to 4asi 15 asd to 62 asd 1asi to 6 asi 15 asd to 95 asd Solution Agitation Mild Air (blower) or mixer Mild Air (blower) or mixer Mild Air (blower) or mixer Anode-to-Cathode Area 1:1 to 3:1 1:1 to 3:1 1:1 to 3:1 Lead-7%Tin or Lead 6% Antimony Lead-7%Tin Lead-7%Tin or Lead 6% Antimony Temperature °F/°C Anode Material Table 1, Operating Conditions As operating temperatures rise, the efficiency of the bath decreases. However, this can be offset by the ability to plate at higher current densities to further gain a faster plating rate. Table 2 shows the efficiency differences between two temperature variables and the resulting efficiency. This effect is even greater with 264

Articles in this issue

view archives of Metal Finishing Guide Book - 2013