Effect of acetate and methanol on the kinetics of total dissolved selenium removal in a chemostat

Elnaz Mohammadi,Susan A. Baldwin

JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY(2024)

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Abstract
BACKGROUNDCarbon (C) source consumption in industrial bioreactors removing soluble selenium (Se) contributes to the operating cost and can influence the rate of removal. This study used a laboratory chemostat to investigate the dependency of the rate of dissolved Se removal on the concentration of acetate and methanol, two C sources used in treatment of Se containing mine-influenced water. It was hypothesized that the rate of dissolved Se removal follows a Monod kinetic model with C source as the limiting substrate.RESULTSA chemostat fed with 25 mg-selenate-Se L-1 and acetate as C source at different concentrations operated over a range of hydraulic retention times (HRTs) achieved maximal removal of 99.7% dissolved Se at an HRT of 1.5 days [rate 16.7 mg-Se (L day)-1]. When methanol was fed into the chemostat as the C source instead of acetate, the extent and rate of removal were much less [65% at an HRT of 6 days, rate 2.7 mg-Se (L day)-1]. Carbon source consumption per mole of dissolved Se removed was not constant and exceeded stoichiometric estimates. Monod kinetic parameters for the Dechloromonas/Ralstonia consortium growing on acetate were estimated as KC$$ {K}_{\mathrm{C}} $$= 3.36 mg-C L-1 and YX/Cqmax,C$$ {Y}_{X/\mathrm{C}}\ {q}_{\max, \mathrm{C}} $$= 0.70 L day-1. The Methylophilaceae consortium growing on methanol did not exhibit Monod kinetic growth.CONCLUSIONSUsing acetate as a C source achieved greater efficiency of dissolved Se removal than when methanol was used. Total dissolved Se removal rate was dependent on acetate only at low concentrations and when the HRT was close to washout. However, total dissolved Se removal rate was strongly dependent on HRT when methanol was used. (c) 2024 The Authors. Journal of Chemical Technology and Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry (SCI).
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Key words
selenium,chemostat bioreactor,suspended-growth,continuous flow reactor,Monod kinetic model,hydraulic retention time,bacterial consortium
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