posted on 2018-08-22, 00:00authored byS. Curcio, F. Petrosino, M. Morrone, G. De Luca
In
the present paper,
an improved multiscale modeling aimed at
describing membrane fouling in the UltraFiltration (UF) process was
proposed. Some of the authors of this work previously published a
multiscale approach to simulate ultrafiltration of Bovine Serum Albumin
(BSA) aqueous solutions. However, the noncovalent interactions between
proteins and the membrane surface were not taken into account in the
previous formulation. Herein, the proteins-surface interactions were
accurately computed by first-principle-based calculations considering
also the effect of pH. Both the effective surface of polysulfone (PSU)
and the first layer of proteins adsorbed on the membrane surface were
accurately modeled. Different from the previous work, the equilibrium
distance between proteins was calculated and imposed as lower bound
to the protein–protein distances in the compact deposit accumulated
on the membrane surface. The computed BSA surface charges were used
to estimate the protein potential and the charge density, both necessary
to formulate a forces balance at microscopic scale. The protein surface
potential was compared with Z-potential measurements of BSA aqueous
solution, and a remarkable agreement was found. Finally, the overall
additional resistance, as due to both the compact and loose layers
of the deposit, was computed, thus allowing the final transition to
a macroscopic scale, where an unsteady-state mass transfer model was
formulated to describe the behavior of a typical dead-end UF process.
A good agreement between simulated and experimental permeate flux
decays was observed.