The fouling tendencies of seven commercial antifoam agents used with m
icrofiltration membranes were investigated in a stirred cell. Paramete
rs such as viscosity, oil droplet size distribution, contact angle, wo
rk of adhesion (W-a), membrane type, operating pressure, and feed conc
entration were examined. The results show that a silicone-based antifo
am, G832, gave a significantly lower flux (less than or equal to 100 L
h(-1) m(-2)) than the polypropylene glycol antifoam PPG2000 (1500-250
0 L h(-1) m(-2)) over the concentrations from 0.5 to 4.0 mt L-1 at.50
kPa, 700 rpm, and 25 degrees C. The significantly lower flux attained
by the antifoam G832 was attributed to a number of factors, such as it
s greater viscosity (1.25 x 10(-3) kg m(-1) s(-1) compared with 1.05 x
10(-3) kg m(-1) s(-1) for PPG2000), a smaller average oil droplet siz
e (0.28 vs. 0.65 Cim) comparable to the membrane pore size distributio
n (0.26-0.62 Crm), a higher contact angle (98 vs. 51 degrees); and a s
ignificantly larger value of work of adhesion (26.0 vs, 0.81 mN m(-1))
. The different magnitudes of membrane adsorption by these antifoam ag
ents, as reflected by their values of work of adhesion, were also obse
rved in the field emission scanning electronic microscopy photographs.
In terms of membrane type, the inorganic Anopore alumina membrane was
found to offer a higher PPG flux than the organic Millipore polyvinyl
difluoride (PVDF) membranes (both hydrophilic and hydrophobic). Furth
ermore, the mixed-type antifoams (B5600, B426, and G832) were found to
give an increased hydraulic resistance and fouling percentage with an
increase in pressure or feed concentration. Conversely for PPG2000, a
reduction of the hydraulic resistance and fouling percentage was obse
rved with increases of these two parameters. (C) 1997 John Wiley & Son
s, Inc.