The flux behavior of ceramic membranes with different pore sizes (0.2, 0.1
and 0.02 mu m) was examined during dead-end membrane filtration of depectin
ized control (CTJ) and ascorbic acid treated (AAJ) apple juices. A new mode
l based on an expanded exponential relationship was developed. The model re
presented the flux with precision over the entire filtration process for bo
th juice types and all membrane pore sizes. Two parameters, A and B, provid
ed a measure of the rate of flux decline. The same approach was used to mod
el the permeate flux of CTJ for various 0.2 mu m pore size polymeric membra
ne materials operated in a dead-end mode, and for tubular ultrafiltration m
embranes of different pore sizes (9, 20 and 100 kDa) operated in crossflow
mode. (C) 2000 Elsevier Science Ltd. All rights reserved.