Ozone transfer was investigated using various oxide ceramic membranes and d
ifferent process parameters. The ozone mass transfer per contactor volume t
hrough hydrophilic membranes was in the same order of magnitude as conventi
onal bubble contacting. The pressure differential between the gaseous and a
queous phase as well as the membrane material's microstructure was found to
widely determine the transfer rate. A hydrophobic coating of the membrane
surface led to a considerable increase in transfer. Bubble free ozone conta
cting with porous ceramic is a possible approach for the ozonation of probl
ematic wastewaters susceptible of excessive foam formation.