A theoretical investigation of particle deposition onto a permeable surface of a tubular membrane is presented. The mass transport mechanisms are mathematically expressed using the two-dimensional convective diffusion equation. A numerical scheme is presented to solve the two-dimensional convective diffusion equation at the steady state for the case of nonuniform permeation velocity. This equation is solved numerically using a finite difference method. The numerical prediction of mass transfer in the mass boundary requires the use of a very dense grid. The concentration pro-files along the membrane surface and the mass boundary layer are predicted. The effect of the Reynolds number, the wall Reynolds number and the Schmidt number were investigated. Correlations for the concentration boundary layer thickness delta(c)/D = 2(z/D)(0.33) (ReSc)(-0.33) Re-w(-0.3) (1 - 0.4377 Sc-0.0018 Re-w-(0.1551)), and for the Sherwood number Sh = 1.230 [(D/z) ReSc](0.33) (1 + 0.010 Re-0.125 SC1.055 Re-w(1.132)) based on the predicted values of the solute concentration profiles, are proposed, in the operating condition ranges 300 < Re < 1000, 0.02 < Re-w < 0.3 and 600 < Sc < 3200.