Abstract

We show novel results addressing the problem of synthesizing a metabolite of interest in continuous bioreactors through resource allocation control. Our approach is based on a coarse-grained self-replicator dynamical model that accounts for microbial culture growth inside the bioreactor, and incorporates a synthetic growth switch that allows to externally modify the RNA polymerase concentration of the bacterial population, thus disrupting the natural process of allocation of available resources in bacteria. Further on, we study its asymptotic behavior using dynamical systems theory, and we provide conditions for the persistence of the bacterial population. We aim to maximize the synthesis of the metabolite of interest during a fixed interval of time in terms of the resource allocation decision. The latter is formulated as an Optimal Control Problem which is then explored using Pontryagin's Maximum Principle. We analyze the solution of the problem and propose a sub-optimal control strategy given by a constant allocation decision, which eventually takes the system to the optimal steady-state production regime. On this basis, we study and compare the two most significant steady-state production objectives in continuous bioreactors: biomass production and metabolite production. For this last purpose, and in addition to the allocation parameter, we control the dilution rate of the bioreactor, and we analyze the results through a numerical approach. The resulting two-dimensional optimization problem is defined in terms of Michaelis-Menten kinetics, and takes into account the constraints for the existence of the equilibrium of interest.

Highlights

  • Microorganisms continuously have to contend with environmental changes in nature, and so they have evolved to adapt their physiology to cope with this unsteadiness

  • Microorganisms like bacteria exhibit great genetic variability, which is the main driver of natural selection, a phenomenon that depends on the continuous mutations in living populations

  • Based on the presented works, we show novel results addressing the problem of bacterial resource allocation in the Continuous Stirred-Tank Reactor (CSTR) framework

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Summary

Introduction

Microorganisms continuously have to contend with environmental changes in nature, and so they have evolved to adapt their physiology to cope with this unsteadiness. Examples of self-replicator models in continuous bioreactors can be found in some recent works: In [16], authors use a coarse-grained self-replicator kinetic model of Saccharomyces cerevisiae’s in a continuous bioreactor to investigate the trade-off between respiratory and fermentative metabolism, showing that optimal strategies are ‘pure’ metabolic strategies (e.g., either respiration of fermentation, but not respiro-fermentation) Likewise, it is rather classical in the continuous bioreactor scheme to maximize a certain performance measure (i.e., biomass production) in terms of the operational parameters related to the setup, such as dilution rate and/or concentration of the substrate inflow [17,18,19,20,21]. The resulting two-dimensional optimization problem is defined in terms of Michaelis-Menten kinetics with the parameter values of [4], and taking into account the constraints for the existence of the equilibrium of interest

Self-replicator model
Asymptotic behavior
Mass conservation
Limiting systems
Global analysis
Metabolite production
Kinetic’s definition
Dynamic optimization problem
Static optimization problem
Findings
Discussions
Full Text
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