Rectifiers for the Plating Industry
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Calculating Electroless Nickel Square Footage

Matthew Wojcik of Coventya Inc. offers advice for calculating the proper square footage of work that can be processed through an EN bath.

Matthew Wojcik, senior R&D chemist, Coventya Inc.

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electroless nickel, plating

Matthew Wojcik is a senior R&D chemist at Coventya Inc. Visit coventya.com

Q: We are a plating shop looking to expand our capabilities in electroless nickel. I understand that EN baths have a finite life so if we install a 200 gallon tank, how much work (sq. ft.) would be we able to process out of one bath? We typically plate to a thickness of 0.0005 inches of a high phosphorous system for our customers.

A: Before we get into the calculations, here is some background information that is required:

  1. Traditional high phosphorous (i.e. > 10.5% w/w P) systems operate at 6 g/L (or 0.8 oz/gal) of Ni metal in the working solution. This is the amount of nickel to be depleted per 1 MTO cycle.
     
  2. Below is the visual representation of what we are looking to calculate:
    plating, metal plating,
    As we are trying to calculate for the square footage, or the area, that can be processed through a solution, you would also need to consider the thickness of your final product. As the thickness increases per part, the total amount of nickel eligible to be plated decreases, thus decreasing the amount of area that can be plated.
     
  3. For this example, a high phosphorous EN system produces a deposit with 11% P and 89% Ni. This will result in a deposit density of 7.8 g/cm3. See below for the density of various EN deposits based on phosphorous concentration.

    Deposit
    % Phosphorous

    Deposit
    % Nickel

    Deposit Density (g/cm3)

    0

    100

    8.9

    1

    99

    8.8

    2

    98

    8.7

    3

    97

    8.6

    4

    96

    8.5

    5

    95

    8.4

    6

    94

    8.3

    7

    93

    8.2

    8

    92

    8.1

    9

    91

    8.0

    10

    90

    7.9

    11

    89

    7.8

    12

    88

    7.7

    13

    87

    7.6

    *Mallory, G.; Hajdu, J. Electroless Plating: Fundamentals and Application; Noyes Publications: New York, NY, 1990.

  4. Calculation of the conversion factor to achieve ft2/gal/MTO:
    a.    In order to convert the units from the information that you generated for your deposit, a conversion factor needs to be generated to ensure the units align. This factor is generated below:

    plating

Calculation of high phosphorous example (ft2/gallon/MTO) from the information provided:

plating


Therefore, for a 200-gallon tank, you would be able to process 553.2  ft2/MTO.

The end result will be a good estimate of the amount of work that can be processed under ideal conditions in the bath per MTO. The maximum MTO that you will be able to achieve with the bath will depend on the properties of the end customer requests, as well as, the type(s) of substrate being processed. As the bath continues to age, the accumulation of by-products (e.g. Na, SO4 and orthophosphate) and contaminants will begin to impact the deposition process and therefore the coating integrity.

Additional conditions may also affect the square footage of work that can be processed in an EN bath. These include, but are not limited to:

  1. Operating the bath outside recommended operating conditions. Doing so may have an effect on the amount of nickel deposited, resulting in a less efficient bath.
  2. Plate-out in the tank. As you plate nickel on racks, barrels, the tank, etc., you are consuming nickel in your tank, thus depleting the amount that can be utilized for the intended plating operation.
  3. Over-plating the parts. If the desired thickness is not consistently being reached, you may observe a decrease in the amount of work that can be processed through your tank, as there will be excess depletion per MTO not being accounted for in the calculations.

In conclusion, calculating the proper square footage of work that you would be able to process through your EN bath is key for determining the proper costing for a job, as well as, providing a reference for proper bath performance. If you begin to notice large deviations from the expected optimal yield, it could be an indication of possible loss of efficiency due to idling of the plating tank for long periods of time without work or unaccounted for nickel plate-out. These can be areas of possible process improvement to reduce operating costs. Your electroless nickel supplier should be able to supply you with a handy calculator to generate these values for you in a simple and fast way.

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