“…The air and salt solution flows are assumed to be laminar and fully developed for the practical operating range of RAMEEs, therefore the convective heat and mass transfer coefficients for a given design are constant since the Nusselt number for a fully developed laminar flow is constant and is equal to 8.24 for a uniform heat flux in a parallel plate channel [26].Thus, U m /U is only a function of air channel thickness, th, (since for a constant Nusselt number, the convective heat and mass transfer coefficients change with th) the thickness of membrane, d, and the heat conductivity and mass conductivity of the membrane, k and k m . Therefore, for a given membrane and air channel thickness the ratio of U m to U is constant Therefore, for a given membrane and air channel thickness, the ratio of U m to U is constant provided that analogy between heat and mass transfer applies in the airstream and the flow configuration (counterflow in this paper) remains constant [27,28]. For other conditions and designs, the heat and mass transfer coefficients and the ratio of Um to U may change [27][28][29][30][31][32].…”