The major sweet potato root protein, sporamin (which comprises about 8
0-90% of the total protein mass in the sweet potato) easily foams in a
bubble/foam-fractionation column using air as the carrier gas. Contro
l of that foam fractionation process is readily achieved by adjusting
two variables bulk solution pH and gas superficial velocity. Varying t
hese parameters has an important role in the recovery of sporamin in t
he foam. Changes in the pH of the bulk solution can control the partit
ioning of sporamin in the foam phase from that in the bulk phase. A ch
ange in pH will also affect the amount of foam generated. The pH varie
d between 2.0 and 10.0 and the air superficial velocities (V-0) ranged
between 1.5 and 4.3 cm/s. It was observed in these ranges that, as th
e pH increased, the total foamate volume decreased, but the foamate pr
otein (mainly sporamin) concentration increased. On the other hand, th
e total foamate volume increased significantly as the air superficial
velocity increased, but the foamate concentration decreased slightly.
The minimum residual protein concentration occurred at pH 3.0 and V-0
= 1.5 cm/s. On the other hand, the maximum protein mass recovery occur
red at pH 3.0 and at V-0 = 4.3 cm/s.