A Capillary Flow Model for Filtration Lei Pan, Kaiwu Huang and Roe-Hoan Yoon* Center for Advanced Separation Technologies Virginia Tech, Blacksburg, VA 24061, United States ABSTRACT Darcy’s law has been used extensively to model cake filtration. It is a macroscopic model derived for fluid flow through a bed of particles, with particle size being an important parameter. In the present work, we have derived a capillary flow model to study the effect of microscopic parameters such as capillary radius, boundary layer slip, and disjoining pressure that may be important for dewatering layer-structured minerals. Our two-phase flow model assumes that a filter cake consists of multiple straight capillaries of a uniform radius (r) as follows, dV AP 2 dt [8L / kr (1 b / 4r ) Rm ] in which V is the volume of liquid with a viscosity flowing through a filter of thickness L and a cross sectional area A; k is the fraction of A due to capillaries; Rm is the medium resistance; P is the pressure drop across the filter cake and a filter medium; and b is the slip length at the solid/liquid interface. These model parameters have been determined iteratively using the experimental data obtained on kaolin clay with a 2 m top size. As shown in Figure 1, the experimental data obtained in pure water can be fitted with r = 49.5 nm and other parameters shown in the figure. The data obtained in the presence of dodecylaminiumhydrochloride (DAH) can be fitted with r = 82 nm assuming that b = 0 and k = 0.63. These results suggest that the improved dewatering kinetics observed with DAH may be due to the increase in capillary radius, which in turn can be attributed to the hydrophobic coagulation associated with the increase in water contact angle () of clay (Xu and Yoon, 1990). The model is useful to study the effects of colloidal forces, cake structure, and medium structure on dewatering kinetics. Reference: Xu, Z. and Yoon, R.-H., 1990, A study of hydrophobic coagulation, J Colloid Interf. Sci., 134, 427-434. Fig. 1. Effect of DAH on the rate of filtration for kaolinite clay at a driving pressure of 15 psi. KEYWORDS Modelling, Filtration, Mature fine tailing, Kaolinite, Dewatering aids, Hydrophobic