A series of studies are currently being undertaken to develop a model that can be used to
accurately predict the evolution of the trans-membrane pressure over time in a full-scale
submerged membrane system. These studies investigate the effects of the hydrodynamic
conditions and the configuration of submerged hollow fiber membrane systems on
membrane fouling. The results from one of these studies indicated that the increase in the
trans-membrane pressure during one filtration cycle, could be modeled using a relatively
simple exponential relationship that was a function of reversible and irreversible fouling
coefficients. The present study was undertaken to determine if this exponential
relationship could be used to accurately describe the evolution of the trans-membrane
pressure in a submerged membrane system during successive filtration cycles.
The fraction of the total fouling that was initially defined as reversible (i.e. defined by a
reversible fouling coefficient) could consolidate and produce irreversible fouling over
time. The extent of consolidation appeared to be directly related to the duration of a
filtration cycle (i.e. time between maintenance cleaning cycles). For relatively short
filtration cycles, the extent of consolidation was negligible. Therefore, when a membrane
system was operated with relatively short filtration cycles, the evolution in the transmembrane
pressure over time could be modeled using a relatively simple exponential
relationship that is a function of three parameters: the pseudo-steady-state permeate flux
(JSS), an irreversible fouling coefficient (KI) and a reversible fouling constant (kr).
Additional studies are currently being conducted to investigate the effects of different raw
water sources on the parameters (i.e. JSS, KI, and kr) that describe the evolution in the
trans-membrane pressure over time in submerged membrane systems. Includes 12 references, tables, figures.