A novel technique was tested for reducing tubular mineral membrane fouling
by injecting gas into a cross-flow stream. The injected gas is thought to f
orm complex hydrodynamic conditions inside the microfiltration module, whic
h increase the wall shear stress, preventing the membrane fouling and enhan
cing the microfiltration mass transfer. The experimental study was carried
gut with biologically treated wastewater filtered through a tubular inorgan
ic membrane (Carbosep M14). The flux, monotonously increasing with gas velo
city, was more than tripled. New dimensionless quantities of shear stress n
umber and resistance number were developed by generalisation of the dimensi
onal analysis already carried out for the steady state flux of classical un
sparged cross-flow filtration. A unique formalism allowed then interpreting
the experimental results of both classical diphasic filtration and sparged
filtration. The main limiting mass transport process was due to the solid
content.