2008 Annual Meeting

(677a) Dynamic Flux Balance Models for Simulation and Optimization of Saccharomyces Cerevisiae Fed-Batch Cultures

Authors

Hjersted, J. L. - Presenter, University of Massachusetts Amherst
Henson, M. A., University of Massachusetts Amherst
We have previously developed dynamic flux balance models for
prediction of cellular growth and metabolic product formation rates
in Saccharomyces cerevisiae batch and fed-batch cell
cultures. These models couple steady-state stoichiometric balances
on intracellular metabolites with dynamic extracellular balances on
biomass, substrates, and metabolic byproducts through time-varying
substrate uptake rates. In this contribution, we present the results
of Saccharomyces cerevisiae fermentation experiments
designed to evaluate the dynamic flux balance model predictions. We
utilized a compartmentalized, genome-scale metabolic network to
describe intracellular metabolism and simple Michaelis-Menten
kinetics for the glucose and oxygen uptake rates. Kinetic parameters
for the substrate uptake and the intracellular stoichiometric
coefficients representing growth and non-growth associated energy
requirements were estimated by nonlinear least squares optimization.
A series of batch and fed-batch experiments demonstrated that the
dynamic flux balance model was able to produce accurate substrate,
biomass, and extracellular product concentration profile predictions
over a wide range of fermentation conditions. The model was
incorporated with a bi-level dynamic optimization scheme to compute
fed-batch operating policies for optimal ethanol production in batch
and fed-batch cultures. Experimental implementation of the optimal
policies showed good agreement with the in silico
predictions.