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The corrosion rate was calculated on the basis of coating mass loss with respect to time.
Based on the amount of coating mass as a function of process variables and the potential-time measurement, a pictorial model is proposed for the deposition of zinc phosphate coating.
This preferential spraying of small particles in the mechanical mixer indicates that the size dependence of coating mass growth rate is a strong function of the equipment geometry and particle flow field.
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The effects of erodent incrustation (SEM/EDS mapping) and oxidation of metallic coating (mass weight) were considered.
The experimental results indicated that the coating mass of particles is directly proportional to the liquid flow rate of the coating solution and inversely proportional to the air flow rate.
The substrates were fully covered with the coatings after PCC treatment at 70 °C for 30 and 45 min with the coating mass of 4.08 and 6.48 g/m2, respectively.
In this work, an experimental investigation was conducted using Response Surface Methodology (RS M to optimize the coating mass of particles in a top-spray fluidized bed coating.
The factor for a quantitative reassessment of the criticality and risk priority is the coefficient of variation, which represents the coating mass uniformity.
This will afford a coating mass thickness of approximately 0.045 g cm−2.
For unimodal core particle distributions, the coating mass coefficient of variation was proportional to t−0.5 where t is the coating time, consistent with both the PB model and other published coating models.
The properties of shear-mode FBAR device adopted for the coating mass detection are demonstrated in Figure 9.
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