Table 6 Analyzed kinetic models.

From: Removal of organic matter and nutrients from hospital wastewater by electro bioreactor coupled with tubesettler

Parameter

Model analyzed

Equation used

Linearized equation

Kinetic parameters obtained

R2 value

COD

1st order

\(\frac{{ - {\text{d}}s}}{{{\text{d}}t}} = \frac{Q}{v}\left( {s_{0} - s_{e} } \right) - k_{1} s_{e}\)

\(\frac{{s_{0} }}{{s_{e} }} - 1 = k_{1} HRT\)

K1 = 1.213

0.761

Grau 2nd order Model

\(\frac{{ - {\text{d}}s}}{{{\text{d}}t}} = \frac{{k_{2} xs_{e} 2}}{{s_{0}^{2} }}\)

\(\frac{{s_{0} }}{{s_{0} - s_{e} }}HRT = {\raise0.7ex\hbox{${HRT - S_{0} }$} \!\mathord{\left/ {\vphantom {{HRT - S_{0} } {k_{2} x}}}\right.\kern-\nulldelimiterspace} \!\lower0.7ex\hbox{${k_{2} x}$}}\)

Ks = 10–05

0.982

Modified Stover-Kincanna model

\(- \frac{{{\text{d}}s}}{{{\text{d}}t}} = \frac{Q}{v}\left( {\frac{{s_{0} - s_{e} }}{{s_{0} }}} \right) = \frac{{U_{M} \frac{{Qs_{0} }}{v}}}{{k_{B} + \frac{{Qs_{0} }}{v}}}\)

\(\frac{v}{{Q\left( {s_{0} - s_{e} } \right)}} = \frac{{k_{B} v}}{{U_{M} s_{0} Q}} + \frac{v}{{U_{M} }}\)

KB = 0.35

UM = 1.73

0.978

Monod Model

\(- \frac{{{\text{d}}s}}{{{\text{d}}t}} = \frac{Q}{v}\left( {\frac{{s_{0} - s_{e} }}{{s_{0} }}} \right) = \frac{{U_{M} \frac{{Qs_{0} }}{v}}}{{k_{B} + \frac{{Qs_{0} }}{v}}}\)

\(\frac{vx}{{Q\left( {s_{0} - s_{e} } \right)}} = \frac{{k_{s} }}{{ks_{e} }} + \frac{1}{k}\)

K = 0.062

Ks = 0.073

0.991