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. 2009 Dec 22;6:30. doi: 10.1186/1742-4682-6-30

Table 1.

Model parameters used in this study

parameter symbol value unit
growth rate, chelator μ1 12.3 d-1
growth rate, non-chelator μ2 12.3 d-1
half-saturation concentration, chelator k1 3.7 μM
half-saturation concentration, non-chelator k2 3.7 μM
decay rate, chelator d1 0.49 d-1
decay rate, non-chelator d2 0.49 d-1
yield coefficient, chelator Y1 0.6003 -
yield coefficient, non-chelator Y2 0.6003 -
maximum biomass density, chelator N 104 gm-3
maximum biomass density, non-chelator R 104 gm-3

chelation rate β 1.92 Inline graphic
pyoverdine production rate δ 2.56 ODPd-1
pyoverdine inhibition concentration S∞ 0.3762 μM
pyoverdine inhibition exponent n 3 -

biomass motility parameter ϵ 10-12 m2d-1
biomass interface exponent a 4 -
biomass threshold exponent b 4 -
diffusion coefficent of iron in water d(0) 8.64·10-4 m2d-1
diffusion coefficent of iron in biofilm d(1) 7.776·10-4 m2d-1