The generalized suspension viscosity equation utilized in this study was evaluated with both a packing fraction, φn, and a particle interaction coefficient, σ, as a function of suspension blend composition, f2T. The estimation of the packing fraction, φn, in turn, required the further elucidation of the D5/D1 ratio of particle diameter averages. Blend constants developed in this study allowed evaluation of both the Dx/Dy ratio of particle diameter averages as well as the number‐average particle diameter, D1, as a function of the fraction of one suspension in a blend, f2T. These blend constants were shown to be easily evaluated from each individual suspension prior to blending. The viscosity data of Johnson and Kelsey were shown to be generally predicted as a function of the volume composition when a constant particle interaction coefficient, σ, was assumed. However, a better prediction of the results of Johnson and Kelsey was obtained by assuming that the particle interaction coefficient, σ, was a function of the number‐average particle diameter, D1, of the suspension mixture composition. Consequently, a new approach was identified to evaluate the simultaneous effects of small particles to both increase viscosity as a result of increasing particle interaction as well as to decrease viscosity as a result of improving the particle‐size distribution.
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Richard D. Sudduth (1993) studied this question.
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