Performance and stability of an anaerobic fixed bed reactor subjected to progressive increasing concentrations of influent organic matter and organic ... from: Journal of Environmental Management]
Book Details
Author(s)A.K.B. Amorim, M. Zaiat, E. Foresti
PublisherElsevier
ISBN / ASINB000RR7LVC
ISBN-13978B000RR7LV1
MarketplaceFrance 🇫🇷
Description
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Description:
Data on the performance of a horizontal-flow anaerobic immobilized biomass (HAIB) reactor subjected to step increases of organic loading rates (OLR) and to organic shock loads (OSL) are presented and discussed. The tubular reactor (100cm long and 5cm diameter) with a useful volume of 1995mL was filled with polyurethane foam cubic matrices holding immobilized biomass and fed with synthetic wastewater. The reactor was operated at the controlled temperature of 30+/-1^oC and hydraulic retention time of 7h. After about 15 days, the HAIB reactor attained operating stability. Thereafter, it was subjected to step increases of the applied OLR that ranged from 6.8 to 18.8kgCOD/m^3d. After steady state had been achieved at each step, OSL corresponding to approximately three times the operating OLR were applied for 7h. No disturbance was observed due to the step increase in OLR. An increase in effluent chemical oxygen demand (COD) and volatile fatty acids (VFA) concentrations and a decrease in the percentage of methane in the biogas were observed due to OSL applications. However, stability of the monitoring parameters was always restored approximately 17h after the application of OSL for all conditions tested.
Description:
Data on the performance of a horizontal-flow anaerobic immobilized biomass (HAIB) reactor subjected to step increases of organic loading rates (OLR) and to organic shock loads (OSL) are presented and discussed. The tubular reactor (100cm long and 5cm diameter) with a useful volume of 1995mL was filled with polyurethane foam cubic matrices holding immobilized biomass and fed with synthetic wastewater. The reactor was operated at the controlled temperature of 30+/-1^oC and hydraulic retention time of 7h. After about 15 days, the HAIB reactor attained operating stability. Thereafter, it was subjected to step increases of the applied OLR that ranged from 6.8 to 18.8kgCOD/m^3d. After steady state had been achieved at each step, OSL corresponding to approximately three times the operating OLR were applied for 7h. No disturbance was observed due to the step increase in OLR. An increase in effluent chemical oxygen demand (COD) and volatile fatty acids (VFA) concentrations and a decrease in the percentage of methane in the biogas were observed due to OSL applications. However, stability of the monitoring parameters was always restored approximately 17h after the application of OSL for all conditions tested.
