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<metadata xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dc="http://purl.org/dc/elements/1.1/"><dc:title>A kinetic study on drinking water denitrification using a membrane bioreactor</dc:title><dc:creator>Petrovič,	Aleksandra	(Avtor)
	</dc:creator><dc:creator>Goršek,	Andreja	(Avtor)
	</dc:creator><dc:creator>Simonič,	Marjana	(Avtor)
	</dc:creator><dc:subject>kinetics</dc:subject><dc:subject>denitrification</dc:subject><dc:subject>drinking water</dc:subject><dc:subject>membrane bioreactor</dc:subject><dc:subject>sucrose</dc:subject><dc:description>This study determines the basic parameters of Monod kinetics for microbial growth within a membrane bioreactor using the Zenon ZeeWeed 10 MBR system. The influent nitrate concentration was kept at 70 ± 2 mg L-1 NO3ˉ. During the experiments a constant concentration of activated sludge was maintained at approximately 0.76 g L-1 under anoxic conditions. Sucrose was added to the activated sludge as a carbon source. The Monod kinetic parameters were calculated by numerical interpolation, by considering experimental data. The maximum specific growth rate of the biomass was determined to be 0.31 h-1, half-saturation constant 5.4 mg L-1, and yield coefficient 0.35 mg biomass mg-1 COD. Afterwards, a dynamic simulation was performed within the calculated parameters. The dynamic concentration profiles for substrate and biomass were determined at different dilution rates within the range of 0.8 to 5 d-1.</dc:description><dc:date>2015</dc:date><dc:date>2016-05-11 03:53:57</dc:date><dc:type>Znanstveno delo</dc:type><dc:identifier>59274</dc:identifier><dc:identifier>ISSN: Y507-8113</dc:identifier><dc:identifier>UDK: 66</dc:identifier><dc:identifier>OceCobissID: 28249383</dc:identifier><dc:identifier>COBISS_ID: 18722838</dc:identifier><dc:identifier>DOI: 10.1515/chem-2015-0112</dc:identifier><dc:identifier>ISSN pri članku: Y507-8113</dc:identifier><dc:identifier>NUK URN: URN:SI:UM:DK:VBRFIUXM</dc:identifier><dc:language>sl</dc:language></metadata>
