Published: CABEQ 25 (4) (2011) 445ā452
Paper type: Original Scientific Paper
A. Rezaee, S. Jorfi and R. D. Cheshmeh Soltani
Abstract
A lab-scale Plexiglas cubic container as a pre-aeration reactor with total volume
of 10 L, and two integrated bioreactors including a moving-bed bioreactor (MBBR)
and a fixed-bed bioreactor with total volume of 30 L separately were used for experimental study. The main purpose was to compare the performance of moving-bed
and fixed-bed reactors for degradation of high organic loading in synthetic wastewater.
Varying organic loadings of 0.5 to 9 kg COD m3 dā1 were applied. Generally, the total
microbial mass in terms of attached biofim and VSS was higher in the MBBR. The
microbial mass in the MBBR increased from 4120 to 4640 mg Lā1 and in the fixed-bed
bioreactor from 4124 to 4564 mg Lā1. The COD removal efficiency in sequencing
runs of operation in moving-bed and fixed-bed bioreactors varied from 96.27 % to
81.27 %, and from 95.2 % to 74.82 % respectively. The data obtained from this study indicate that MBBR, with the applied media in this study, was more efficient than the
fixed-bed bioreactor for biodegradation of organic matter under identical operating conditions.
This work is licensed under a Creative Commons Attribution 4.0 International License
Keywords
moving-bed reactor, fixed-bed reactor, biofilm, organic matter, biodegradation