Based on fermentation data for cyclosporin A production, simple Monod kinetics was proposed for both immobilized and suspended cultures. Higher value of $mu$mas and lower value of Km suggest better catalytic activity of the immobilized cells than the parallel suspended cells. Furthermore, lower Km value in the immobilized cell system indicates higher affinity of the immobilized cells for carbon substrate as compared with the suspended cells. For immobilized cell cultures, these parameters were also utilized for the estimation of effectiveness factor, an indicator for intraparticle mass transfer resistance. Based on simulation studies, optimum radius of celite beads was turned out $100 ~ 500{mu}m$In this simulation work, we examined the influence of biosupport size and immobilized biomass density on diffusional resistance of substrate inside the bead matrix. In order to maintain uniformly distributed cell activities in biosupport, it was essential to determine optimum slze of particle, and then to estimate the most economic loaded biomass content.