The following data as obtained in a batch reactor for the yeast Saccharomyces cerevisiae
t(h) | 0 | 1 | 2 | 3 | 4 | 6 | 8 |
CC(g/dm3) | 1 | 1.39 | 1.93 | 2.66 | 3.7 | 7.12 | 13.7 |
CS(g/dm3) | 250 | 245 | 238 | 229 | 216 | 197 | 94.4 |
CP(g/dm3) | 0 | 2.17 | 5.22 | 9.3 | 15.3 | 34 | 71 |
(dCc/dt) (g/dm3.h) | 0.30 | 0.45 | 0.63 | 0.87 | 1.21 | 2.32 | 4.42 |
Hint: See Chapter 7, section 7.4.
(a) Determine the rate law parameters µmax and Ks, assuming the data can be described by the Monod Equation
[Hint: It might be best to regress your data taking the reciprocal of the Monod equation in the form (CsCc/rg) vs. Cs. See Chapter 7, section 7.4.]
What is the residual sums of squares?
(b). Determine the rate parameters µmax and k, assuming the data can be fit by the Tessier Equation
What is the residual sums of squares?
(b) Determine the rate law parameters µmax, k, and λ, assuming the data can be fit by the Moser Equation
What is the residual sums of squares?
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