Predicting membrane flux decline from complex mixtures using flow-field flow fractionation measurements and semi-empirical theory.
Flow-Field Flow Fractionation (FI-FFF) is an idealization of the cross flow membrane filtration process in that, (1) the filtration flux and crossflow velocity are constant from beginning to end of the device, (2) the process is a relatively well-defined laminar-flow hydrodynamic condition, and (3) the solutes are introduced as a pulse-input that spreads due to interactions with each other and the membrane in the dilute-solution limit. We have investigated the potential for relating FI-FFF measurements to membrane fouling. An advection-dispersion transport model was used to provide 'ideal' (defined as spherical, non-interacting solutes) solute residence time distributions (RTDs) for comparison with 'real' RTDs obtained experimentally at different cross-field velocities and solution ionic strength. An RTD moment analysis based on a particle diameter probability density function was used to extract "effective" characteristic properties, rather than uniquely defined characteristics, of the standard solute mixture. A semi-empirical unsteady-state, flux decline model was developed that uses solute property parameters. Three modes of flux decline are included: (1) concentration polarization, (2) cake buildup, and (3) adsorption on/in pores, We have used this model to test the hypothesis-that an analysis of a residence time distribution using FI-FFF can describe 'effective' solute properties or indices that can be related to membrane flux decline in crossflow membrane filtration. Constant flux filtration studies included the changes of transport hydrodynamics (solvent flux to solute back diffusion (J/k) ratios), solution ionic strength, and feed water composition for filtration using a regenerated cellulose ultrafiltration membrane. Tests of the modeling hypothesis were compared with experimental results from the filtration measurements using several correction parameters based on the mean and variance of the solute RTDs. The corrections used to modify the boundary layer mass transfer coefficient and the specific resistance of cake or adsorption layers demonstrated that RTD analysis is potentially useful technique to describe colloid properties but requires improvements.
Pellegrino
J
J
University of Colorado, Department of Civil, Environmental, and Architectural Engineering, Boulder, CO 80309-0428, USA. john.pellegrino@colorado.edu
Wright
S
S
Ranvill
J
J
Amy
G
G
D000327:Adsorption; D003102:Colloids / Q000737:chemistry; D004058:Diffusion; D005374:Filtration; D031521:Fractionation, Field Flow / Q000379:methods*; D008567:Membranes, Artificial; D008851:Micropore Filters; D008954:Models, Biological; D009994:Osmolar Concentration; D016062:Porosity; D011506:Proteins / Q000378:metabolism; D012822:Silicon Dioxide / Q000737:chemistry; D013997:Time Factors; D018508:Water Purification / Q000379:methods*
D003102:Colloids; D008567:Membranes, Artificial; D011506:Proteins; D012822:Silicon Dioxide