Heat and mass transfer in spacer-filled direct contact membrane distillation were
experimentally investigated and explained in more detail based on the
combination of the thin film theory and boundary layer theory. Experimental
results were used to calculate mass transfer coefficient through the boundary
layer instead of existing Sherwood number correlations or modeling results.
Consequently, the change of direct contact membrane distillation (DCMD)
performance in terms of mass fluxes, temperature polarization coefficient (TPC),
and concentration polarization coefficient (CPC) could be analyzed more clearly
through the fluctuation of mass transfer coefficient through the boundary layer,
and boundary layer thickness. Moreover, the results also revealed that the effect
of membrane pore size on the mass transfer coefficient through the boundary
layer, boundary layer thickness, and internal heat transfer coefficient was
insignificant. In contrast, membrane pore size considerably influenced the
membrane permeability coefficient, TPC, and CPC.
Keywords: Direct contact membrane distillation, thin film theory, boundary layer
theory, heat transfer, mass transfer
