Search

Several cations have been used to study the effect of mineral coagulants on activated sludge properties and membrane fouling in submerged membrane bioreactors (MBRs). The flocculability and settling properties of activated sludge were studied in various concentrations of sodium, potassium, magnesium, calcium, ferrum (in Fe(3+) form), and aluminum. Significant effect of cations and their concentrations on different parameters have been analyzed by 2-way ANOVA. Results showed that multivalent cations induce flocculation in bioreactors while monovalent cations have a detrimental effect on flocculability of activated sludge. The ratio of tight bound extracellular polymeric substances (TB-EPSs) to loosely bound (LB-EPSs) increased with concentration of multivalent cations that was in accordance with enhancement of biosorption in high concentration of multivalent cations. Moreover, these cations improved the settleability and dewatering properties of activated sludge. They also mitigated membrane fouling in the MBRs so that calcium and aluminum reduced membrane fouling to nearly 30%. Simple but useful correlations were developed for description of activated sludge properties based on easy measurable parameters that could be used also for estimation of membrane fouling. It was found that the ratio of TB-EPS to LB-EPS and also flocs size distribution are the main parameters affecting membrane fouling., (Copyright © 2013 Elsevier B.V. All rights reserved.)

A laboratory stirred tank bioreactor with six single and dual-impeller configurations was tested to obtain the optimum operating conditions for future biological processes. Six impeller combinations consisting of three basic impeller types, namely Rushton turbine (RT), pitched 4blade (P4B) and pitched 2blade (P2B) downward flow were investigated in 1.77 L bioreactor working volume. Power consumption and gas holdup measurements were taken over a range of 100-1000 rpm of stirring speed and 1-5 Lmin-1 of air flowrates, for all the six combinations consisting of any single and dual impellers. Using predicted data some empirical correlations were derived which present relations in estimation of power consumption in stirred tanks with various impeller configurations. Electrical measurement method was use to determine the power drown in the stirred bioreactor. Gas hold-up increased with an increase in stirring speed and superficial gas velocity for all the impellers employed. The number and type of impellers in stirred bioreactor had considerable influence on gas hold-up behavior of the stirred bioreactor. Besides, Rushton turbine-dual Impeller gave comparably maximum gas hold-up, but at significantly higher power consumption levels. The proposed correlations offered good agreement with the experimental data. [ABSTRACT FROM AUTHOR]