The anaerobic fixed film reactors (AFFR), containing a mixed populatio
n of bacteria immobilized on the surfaces of expanded-clay support med
ium, have been successfully applied in the simulation of high-strength
trade effluent treatment. This paper presents residence time distribu
tion (RTD) studies to investigate the hydrodynamic characteristics in
the packed bed of this novel type of reactor under the mixing effects
of an effluent recycle stream. The results show that the flow pattern
is characterized by various extents of back-mixing as predicted by the
dispersion model. An effluent recycle at a rate equivalent to replaci
ng the liquid content of the AFFR three times per hour achieved a larg
e amount of dispersion in the packed bed. The AFFR without recycle had
an intermediate amount of dispersion. This study shows that treatment
performance of AFFRs and the cause of reactor failure are related to
the effects of the effluent recycle in diluting and distributing the o
rganic constituents of the trade effluent. Copyright (C) 1996 IAWQ. Pu
blished by Elsevier Science Ltd.