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[Preprint]. 2024 Oct 17:2024.10.14.618235. [Version 1] doi: 10.1101/2024.10.14.618235

Extended Data Table 2. Best estimate parameter values used for the biomolecular model (Eqn. S1).

Each parameter is listed with a brief explanation of its meaning and the value used for all simulations within this work. For parameters that were not assigned a specific value (R1,in and R2,in, a range is provided in closed brackets to indicate the sample space of values used for figure generation. Parameters used for discrete time simulations were inferred from a set of experimental data using a nonlinear optimization algorithm in MATLAB. Parameters specific to the chemostat simulations were manually selected.

Parameter Interpretation Value
μ1,max Maximum specific growth rate of ΔtyrA 0.3750
μ2,max Maximum specific growth rate of ΔpheA 0.8817
k13 Saturation constant for glucose consumption by ΔtyrA 1.9620
k23 Saturation constant for glucose consumption by ΔpheA 4.5814
k12 Saturation constant for tyrosine consumption by ΔtyrA 2.0413
k21 Saturation constant for phenylalanine consumption by ΔpheA 6.9279
q13 Yield quotient for ΔtyrA biomass from glucose 5.4112
q23 Yield quotient for ΔpheA biomass from glucose 4.1842
q12 Yield quotient for ΔtyrA biomass from tyrosine 37.7558
q21 Yield quotient for ΔpheA biomass from phenylalanine 46.5086
q11 Maximum production rate of phenylalanine by ΔtyrA 20.4518
q22 Maximum production rate of tyrosine by ΔpheA 11.3321
k1 Saturation constant for phenylalanine production by ΔtyrA 10.7868
k2 Saturation constant for tyrosine production by ΔpheA 2.4787
n1 Hill coefficient for phenylalanine production by ΔtyrA 1.6251
n2 Hill coefficient for tyrosine production by ΔpheA 6.7650
D Dilution rate of the chemostat 0.1000
R1,in Concentration of phenylalanine in the feedstock [0, 200]
R2,in Concentration of tyrosine in the feedstock [0, 200]
R3,in Concentration of glucose in the feedstock 11.1111