An Improved Probing Controller for Substrate Feeding in Fed-Batch Cultures of E. Coli: Simulations and Experiments

2001 ◽  
Vol 34 (5) ◽  
pp. 213-218
Author(s):  
M. Åkesson ◽  
P. Hagander ◽  
J.P. Axelsson
2019 ◽  
Vol 18 (1) ◽  
Author(s):  
Renaldas Urniezius ◽  
Arnas Survyla ◽  
Dziugas Paulauskas ◽  
Vladas Algirdas Bumelis ◽  
Vytautas Galvanauskas

Abstract Background The focus of this study is online estimation of biomass concentration in fed-batch cultures. It describes a bioengineering software solution, which is explored for Escherichia coli and Saccharomyces cerevisiae fed-batch cultures. The experimental investigation of both cultures presents experimental validation results since the start of the bioprocess, i.e. since the injection of inoculant solution into bioreactor. In total, four strains were analyzed, and 21 experiments were performed under varying bioprocess conditions, out of which 7 experiments were carried out with dosed substrate feeding. Development of the microorganisms’ culture invariant generic estimator of biomass concentration was the main goal of this research. Results The results show that stoichiometric parameters provide acceptable knowledge on the state of biomass concentrations during the whole cultivation process, including the exponential growth phase of both E. coli and S. cerevisiae cultures. The cell culture stoichiometric parameters are estimated by a procedure based on the Luedeking/Piret-model and maximization of entropy. The main input signal of the approach is cumulative oxygen uptake rate at fed-batch cultivation processes. The developed noninvasive biomass estimation procedure was intentionally made to not depend on the selection of corresponding bioprocess/bioreactor parameters. Conclusions The precision errors, since the bioprocess start, when inoculant was injected to a bioreactor, confirmed that the approach is relevant for online biomass state estimation. This included the lag and exponential growth phases for both E. coli and S. cerevisiae. The suggested estimation procedure is identical for both cultures. This approach improves the precision achieved by other authors without compromising the simplicity of the implementation. Moreover, the suggested approach is a candidate method to be the microorganisms’ culture invariant approach. It does not depend on any numeric initial optimization conditions, it does not require any of bioreactor parameters. No numeric stability issues of convergence occurred during multiple performance tests. All this makes this approach a potential candidate for industrial tasks with adaptive feeding control or automatic inoculations when substrate feeding profile and bioreactor parameters are not provided.


2013 ◽  
Vol 40 (3-4) ◽  
pp. 335-343 ◽  
Author(s):  
J. Ruiz ◽  
A. Fernández-Castané ◽  
C. de Mas ◽  
G. González ◽  
J. López-Santín

2018 ◽  
Author(s):  
Sujata Vijay Sohoni ◽  
Paras Harendra Kundalia ◽  
Adarsh G. Shetty ◽  
Avinash Vellore Sunder ◽  
Raghavendra P. Gaikaiwari ◽  
...  

AbstractCommercial exploitation of enzymes in biotransformation necessitates a robust method for enzyme production that yields high enzyme titer. Nitrilases are a family of hydrolases that can transform nitriles to enantiopure carboxylic acids, which are important pharmaceutical intermediates. Here, we report a fed-batch method that uses a defined medium and involves growth under carbon limiting conditions using DO-stat feeding approach combined with an optimized post-induction strategy, yielding high cell densities and maximum levels of active and soluble enzyme. This strategy affords strict control of nutrient feeding and growth rates, and ensures sustained protein synthesis over a longer period. The method was optimized for highest titer of nitrilase reported so far (247 kU/l) using recombinant E. coli expressing the Alcaligenes sp. ECU0401 nitrilase. The fed-batch protocol presented here can also be employed as template to produce a wide variety of enzymes with minimal modification, as demonstrated for alcohol dehydrogenase and formate dehydrogenase.


2009 ◽  
Vol 25 ◽  
pp. S223
Author(s):  
A.J. Da Silva ◽  
A.C. Horta ◽  
M. Iemma ◽  
M.T. Novo ◽  
T.C. Zangirolami ◽  
...  

2016 ◽  
Vol 14 (6) ◽  
pp. 1187-1200 ◽  
Author(s):  
Adriana Amicarelli ◽  
Lucía Quintero Montoya ◽  
Fernando di Sciascio

Abstract This work proposes a substrate feeding strategy for a bioprocess integrated with a biomass estimator based in nonlinear filtering techniques. The performance of the proposed estimator and the substrate strategy are illustrated for the δ-endotoxin production of Bacillus thuringiensis (Bt) in batch and fed batch cultures. Nonlinear filtering techniques constitutes an adequate option as estimation tool because of the strongly nonlinear dynamics of this bioprocess and also due to nature of the uncertainties and perturbations that cannot be supposed Gaussians distributed. Biomass estimation is performed from substrate and dissolved oxygen. Substrate feeding strategy is intended to obtain high product concentration. Simulations results along with their experimental verifications demonstrate the acceptable performance of the proposed biomass estimator and the substrate feeding strategy.


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