Abstract

Due to low oxygen solubility and mechanical stirring limitations of a bioreactor, ensuring an adequate oxygen supply during a recombinant Escherichia coli cultivation is a major challenge in process control. Under the light of this fact, a fuzzy dissolved oxygen controller was developed, taking into account a decision tree algorithm presented in the literature, and implemented in the supervision software SUPERSYS_HCDC. The algorithm was coded in MATLAB with its membership function parameters determined using an Adaptive Network-Based Fuzzy Inference System tool. The controller was composed of three independent fuzzy inference systems: Princ1 and Princ2 assessed whether there would be an increment or a reduction in air and oxygen flow rates (respectively), whilst Delta estimated the size of these variations. To test the controller, simulations with a neural network model and E. coli cultivations were conducted. The fuzzification of the decision tree was successful, resulting in smoothing of air and oxygen flow rates and, hence, in an attenuation of dissolved oxygen oscillations. Statistically, the average standard deviation of the fuzzy controller was 2.45 times lower than the decision tree (9.48%). Results point toward an increase in the flow meter lifespan and a possible reduction of the metabolic stress suffered by E. coli during the cultivation.

Highlights

  • Cultivation of Escherichia coli has been extensively studied, focusing on high productivity, oxygen availability, medium composition, acetate production, feeding control strategy, bioreactor type, and operation policy [1,2,3,4]

  • All the findings described suggest that the fuzzy logic is a viable option for dissolved oxygen concentration (DOC) control in an E. coli cultivation, with robust control parameters adjusted by Adaptive Neuro-Fuzzy Inference System (ANFIS)

  • The findings have shown the feasibility of applying fuzzy reasoning for DOC control in a bioreactor

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Summary

Introduction

Cultivation of Escherichia coli has been extensively studied, focusing on high productivity, oxygen availability, medium composition, acetate production, feeding control strategy, bioreactor type, and operation policy [1,2,3,4]. At a certain point, oxygen surplus becomes detrimental for the cultivation (decreasing both biomass yield and specific growth rate and increasing acetate production) [9,10,11]. Regarding the current control strategies, the majority struggles with dissolved oxygen concentration (DOC) peaks and non-smooth behavior of air and oxygen flow rates. In this context, efforts were made in order to improve the DOC control in bioreactors

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