Gas transfer through hollow fiber membranes allows for rapid transfer kinet
ics, high transfer efficiencies, and the ability to precisely control trans
fer rates. Despite these advantages, membrane gas transfer has not been use
d extensively in industrial fermentation or wastewater treatment. Module pl
ugging and biofouling are problematic with current contactor designs, makin
g: membrane gas transfer unattractive for applications where the growth of
microorganisms is encouraged. Recently, a novel rotating contactor configur
ation was designed to give high transfer rates and simultaneously alleviate
these problems. In the rotating contactor configuration, the hollow fiber
membranes are pulled through the water, reducing energy requirements. Solid
s are also able to pass through the fluidized fibers without being filtered
. In addition, the entire fiber length experiences a similar flow velocity.
This makes the control of biological fouling possible. Pilot plant experim
ents on a rotating membrane contactor operated in wastewater are presented.
The performance of the rotating contactor design in such an environment wh
ere the potential for biological fouling exists is evaluated as a function
of operating parameters and time in service. Membrane failures are addresse
d and the transfer performance is compared to other contactor configuration
s and aeration systems.