Recently, a mathematical model for simulating virus trans-Ž port through synthetic barriers gloves, condoms, instrument . Ž sheaths, etc. was developed Myers et al., 1999, hereafter . referred to as MLR99 . The mathematical model comprises a convective-diffusion equation modeling the dominant transport mechanisms away from the barrier surface, and a ''reac-Ž tion-rate'' boundary condition containing information empirically determined for each virusrsuspending-fluidrbarrier-. material combination of interest characterizing the shortrange colloidal force between the virus and the barrier. The reaction-rate boundary condition is derived from the perfect-sink model of adsorption, in which viruses contacting the pore wall are assumed to be irreversibly adsorbed. In comparison with data from experiments using bacterial viruses and latex membranes in a parallel-plate channel, the model considerably underpredicted the rate of virus transmission for residence times that were large compared to the time necessary for the virus to diffuse the height of the channel. Data from transmission experiments reported in MLR99 are re-Ž produced by the square symbols in Figure 1. Data to be dis-. cussed subsequently are also shown. The horizontal axis represents the ratio of the average residence time to diffusion Ž . time for the bacterial virus PRD1 65-nm diameter , where the residence time is the volume of the channel divided by the measured flow rate of suspending fluid, and the diffusion time is the square of the channel half-height divided by the Brownian diffusivity for a spherical particle in an unbounded medium. The vertical axis represents the number of viruses exiting the channel in a short time period divided by the number of viruses entering the channel in the same period. The solid line shows the model predictions obtained through a finite-difference solution to the convective-diffusion equation and reaction-rate boundary condition in the parallel-plate geometry. The higher rate of transmission observed experi-Ž . mentally at larger relative times could reasonably be attributed to reversibilityᎏdesorption of viruses back into suspensionᎏor to saturation of potential virus adsorption sites. A desire to determine the extent to which reversibility and saturation limit the applicability of the perfect-sink model of ᭛ , 7=10 r r r r rmL H , 10 r r r r rmL I , and 10 r r r r rmL ( ) = .The theoertical prediction based on the perfect-sink approximation is given by the solid line.virus adsorption to latex motivated a new set of virus-transport experiments.
ExperimentsIn the experiments, the basic procedure described in MLR99 for model calibration was followed. Latex material was wrapped around two plastic rectangular plates, and a channel was formed by clamping the two plates together with Ž spacers in between. The channel height distance between the . latex films was approximately 100 m, and the width and length of the channel were about 100 and 1,000 times this Ž value, respectively. The suspending fluid was physiologic 0.16