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 | ![]() |
| 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 |
