Optimization and scale up of trickling bed bioreactors for degradation of volatile organic substances

For optimization and scale up of trickling bed bioreactors used in waste gas cleaning following investigations were made: the degradation of toluene was measured in reactors with various volumes and diameter to high ratios. The degradation of toluene was investigated in bioreactors with different carrier materials. It turned out, that the increase of the elimination capacity with the height of the reactor depends on the carrier material. At low gas velocities PU-foam allows higher elimination capacities than pallrings, VSP and DINPAC. On the other hand for PU-foam there is a permanent danger of clogging. The other materials allowed a stable operation for several months. Mass transfer of toluene was studied by absorption experiments in a 100 litre plant without microorganisms. The experiments lead to a henry coefficient of 0,23 (kg/m3)g/(kg/m3)l. Mass transfer coefficients were calculated between 3,6 and 5,2 depending an the space velocity of the gas and the trickling density of the water phase. The degradation of ethyl acetate, toluene and heptane was investigated considering the different water solubility of these substances. Further on degradation of toluene and heptane in several mixtures was investigated. (author)