Time step |
Δt
|
10−3
|
s |
Ad hoc |
Spatial step |
Δx
|
10−4
|
m |
Constrained by CFL numerical condition (34) |
Grid size, N × N
|
N |
100 |
|
|
Fluid dynamics viscosity |
η |
8.9 × 10−4
|
kg · m−1 · s−1
|
61 |
Bacterial vol |
Vb |
3 × 10−18
|
m3
|
Exptl evidence |
Water mass density |
ρ0
|
0.995 × 103
|
kg · m−3
|
61 |
Bacterial mass density |
ρb
|
1.193 × 103
|
kg · m−3
|
57 |
Cellulose mass density |
ρc
|
1.5 × 103
|
kg · m−3
|
Ad hoc |
Maximal bacterial concn |
bsat
|
3 × 1014
|
Cells · m−3
|
Exptl evidence |
Initial concn of bacteria |
b0
|
2 × 1010
|
Cells · m−3
|
Exptl settings |
Diffusion coefficient of bacteria |
Db |
10−10
|
m2 · s−1
|
58 |
Diffusion coefficient of cellulose |
Dc |
5 × 10−11
|
m2 · s−1
|
Ad hoc |
Diffusion coefficient of oxygen |
Do |
10−9
|
m2 · s−1
|
59 |
Diffusion coefficient of pyoverdin |
Dp |
3 × 10−10
|
m2 · s−1
|
Exptl evidence (data not shown) |
Initial oxygen concn |
o0
|
1.5 × 1023
|
Molecules · m−3
|
|
Initial normalized pyoverdin concn |
p0
|
3.36 × 10−5
|
|
Exptl fit |
Initial normalized cellulose concn |
c0
|
10−8
|
|
Ad hoc |
Production of pyoverdin |
β−1
|
1.22 × 10−4
|
s |
Exptl fit |
Production of cellulose |
α−1
|
10−3
|
s |
Ad hoc |
Growth rate of bacteria |
δ |
0.53 |
h−1
|
Exptl fit |
Oxygen consumption/bacterium/s |
γ |
106
|
Molecules · cell−1 · s−1
|
49 |
Vol of cellulose produced/bacterium |
V* = 10 · Vb
|
3 × 10−17
|
m3
|
60 |
Minimal bacterial concn for cellulose production |
b* = bsat/3 |
1014
|
Cells · m−3
|
Exptl evidence |
Boundary condition of oxygen at top |
o0
|
1.5 × 1023
|
Molecules · m−3
|
49 |
Acceleration of gravity |
g |
9.81 |
m · s−2
|
|
Minimal oxygen concn for cellulose and pyoverdin production |
o* |
o0 × 10−1
|
Molecules · m−3
|
Ad hoc |