Mohammadi, F.,
Bina, B.,
Amin, M.M.,
Pourzamani, H.R.,
Yavari, Z.,
Shams, M. Canadian Journal of Chemical Engineering (00084034)96(8)pp. 1762-1769
Alkylphenols (APs) received great attention in the past decade because they were on the priority hazardous substances list. The kinetics of a lab-scale moving bed biofilm reactor (MBBR) that was fed with synthetic wastewater containing 4-NonylPhenol (4-NP) and 4-tert-OctylPhenol (4-t-OP) was investigated in this paper. The MBBR reactor was evaluated under different APs, organic loading rates, and hydraulic retention times (HRT). The substrate removal rate was predicted with the first-order, second-order, Stover-Kincannon, and Monod substrate removal models. 4-NP and 4-t-OP pollutants were removed in the different percentages of 87.1 to 99.9 % and 83.2 to 99.9 %, respectively. Biokinetic parameters, like Y, KS, k, μmax, and kd, that would be favourable to design an MBBR were evaluated. Based on the results, the second-order (Grau), Stover-Kincannon, and Monod models were observed to be the most suitable for this reactor. These models showed high correlation coefficients of about 99.6, 99.1, and 92.9 %, respectively. Consequently, these models could be utilized in anticipating the performance and design of MBBR reactors. © 2017 Canadian Society for Chemical Engineering
