In-situ Determination of Nitrification Kinetics and Performance Characteristics for a Bubble-Washed Bead Filter
James M. Ebelinga and Fredrick W. Wheatonb
a
8470 Lakenheath
Silver Point, TN, 38582 USA
e-mail:
b
Biological Resources Engineering Department
University
of Maryland
College Park, MD 20742 USA
Keywords: nitrification, kinetics, bubble-washed bead filter,
monod kinetics model, performance evaluation
Footnote
International Journal of Recirculating Aquaculture 7 (2006). All
Rights Reserved
© Copyright 2006 by Virginia Tech and Virginia Sea Grant, Blacksburg,
VA USA
ABSTRACT
Intensive recirculating aquaculture systems rely almost exclusively on some
form of fixed film biofilter for nitrification. Currently there is no standardized
way to determine and report biofilter performance to facilitate user selection
among the numerous options. This type of information is critical for the
end user, and also important for both the design engineer and the manufacturer.
In an attempt to address this issue, a simple procedure for estimating nitrification
reaction rate kinetics is described and applied to a bubble-washed bead filter.
Reaction rate kinetics were determined through a series of batch reaction
rate experiments with a commercially available 0.06 m3 (2.0 ft3) bubble-washed
bead filter. Empirical mathematical models for the nitrification of ammonia-nitrogen
to nitrate-nitrogen were developed. The kinetics of nitrification were found
to fit a simple 1st order reaction model, when the ammonia-nitrogen concentration
was less than 1 mg NH4-N/L, and a 0th order reaction when the ammonia-nitrogen
concentration was greater. The exact breakpoint between 1st and 0th order
reaction kinetics was found to be a function of the flow rate. In addition,
the 1st order kinetic reaction rate constants were also a function of the
flow rate, reflecting the influence of high nutrient gradients and associated
higher nutrient gradient across the biofilm. No effect of flow rate was found
for the 0th order reaction rate constants. Kinetic reaction rate parameters,
maximum reaction rates, and half-saturation constants were determined for
the Monod kinetics model as functions of hydraulic loading rate. Based on
these results, an evaluation tool was proposed to help characterize bead
filter performance based on reaction rate kinetics. A series of performance
characteristic curves were developed to show maximum removal rates as a function
of ammonia-nitrogen concentration and flow rates through the bubble-washed
bead filter.
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