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- W2012802185 abstract "A study of the kinetics of the anaerobic digestion of brewery wastewater was carried out using a 1-litre, continuous-flow, completely-mixed, bioreactor operating at 35°C and containing a saponite-immobilized biomass at a concentration of 6·2 g volatile suspended solids (VSS)/litre. The bioreactor worked satisfactorily in a range of hydraulic retention times from 1·2 to 10 days and eliminated more than 95% of the initial chemical oxygen demand (COD) in all instances. Guiot's kinetic model was used to determine the macroenergetic parameters of the system, and showed it to have a yield coefficient for the biomass (Y) of 0·080 g VSS/g COD and a specific rate of substrate uptake for cell maintenance (m) of 0·045 g COD/g VSS day. The experimental results showed the rate of substrate uptake (Rs; g COD/g VSS day), correlated with the concentration of biodegradable substrate (Sb; g COD/litre), through an equation of the Michaelis-Menten type." @default.
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- W2012802185 date "1994-01-01" @default.
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- W2012802185 title "Kinetic study of anaerobic digestion of brewery wastewater" @default.
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- W2012802185 doi "https://doi.org/10.1016/0032-9592(94)80041-3" @default.
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