Parameter | Benchmark value derived from [15] | Case 1 | Case 2 | Case 3 | Case 4 |
---|---|---|---|---|---|
Glucose simulation | Xylose simulation | Sugar mixture simulation | Wheat straw hydrolysate simulation | ||
km, maximal uptake rate (h−1) | 0.35 | – | 1.58 (± 0.042) | 0.54 (± 0.012) | 0.44 (± 0.023) |
km,2, maximal uptake rate when xylose = 0 (h−1) | 0.35 | 2.4 (± 0.15) | – | 0.54 (± 0.018) | 1.26 (± 0.11) |
Ks,glu, affinity constant, glucose (cmol/L) | 0.00029 | 0.01a | – | 0.01a | 0.18 (± 0.043)b |
Ks,glu,2, affinity constant 2, glucose (cmol/L) | – | – | – | 0.01a | 0.01a |
Ks,xyl, affinity constant, xylose (cmol/L) | – | – | 0.0002a | 0.0002a | 0.0002a |
Ks,ara, affinity constant, arabinose (cmol/L) | – | – | – | 0.026 (± 0.004) | 0.034 (± 0.0077) |
Ks,E2, affinity constant enzyme, E2 (cmol/L) | – | – | – | 0.001a | 0.001a |
α, enzyme synthesis rate (h−1) | – | – | – | 0.6a | 0.64 (± 0.085) |
n, Hill coefficient | – | – | – | 2a | 2a |
rcd, cell death rate (h−1) | 0.014 | 0.0027a | 0.0027a | 0.027a | 0.027 (± 0.0039) |
\( k_{\text{L}} a_{{{\text{H}}_{2} }} , \) volumetric mass transfer coefficient for hydrogen (h−1) | 0.26 | 0.44a | 0.44a | 0.44 (± 0.085) | 0.44a |
\( Y_{{{\text{H}}_{2} }} , yield, hydrogen formation from sugar \) | n.c. | n.c. | 0.58 | n.c. |