Concentration-time curves in fed-batch fermentations followed by a batch phase

1988 ◽  
Vol 10 (4) ◽  
pp. 283-284
Author(s):  
Agenor Furigo ◽  
Walter Borzani
Keyword(s):  
Fed Batch ◽  
Batch Phase ◽  
Concentration Time

scholarly journals Self-Inducible Bacillus subtilis Expression System for Reliable and Inexpensive Protein Production by High-Cell-Density Fermentation

2011 ◽  
Vol 77 (18) ◽  
pp. 6419-6425 ◽  
Author(s):  
Marian Wenzel ◽  
Alexander Müller ◽  
Martin Siemann-Herzberg ◽  
Josef Altenbuchner
Keyword(s):  
Bacillus Subtilis ◽  
Protein Production ◽  
Expression System ◽  
Product Yield ◽  
Fed Batch ◽  
Technical Application ◽  
Content Type ◽  
Batch Phase ◽  
Product Yields ◽  
Induction System

ABSTRACTA novel technically compliant expression system was developed for heterologous protein production inBacillus subtiliswith the aim of increasing product yields at the same time as decreasing production costs. Standard systems involve the positively regulatedmanPpromoter of the mannose operon, which led to relatively high product yields of 5.3% (5.3 g enhanced green fluorescent protein [eGFP] per 100 g cell dry weight [CDW]) but required large quantities of mannose to induce the reactions, thus rendering the system's technical application rather expensive. To improve this situation, mutantB. subtilisstrains were used: the ΔmanA(mannose metabolism) strain TQ281 and the ΔmanP(mannose uptake) strain TQ356. The total amount of inducer could be reduced with TQ281, which, however, displayed sensitivity to mannose. An inducer-independent self-induction system was developed with TQ356 to further improve the cost efficiency and product yield of the system, in which glucose prevents induction by carbon catabolite repression. To create optimal self-induction conditions, a glucose-limited process strategy, namely, a fed-batch process, was utilized as follows. The initiation of self-induction at the beginning of the glucose-restricted transition phase between the batch and fed-batch phase of fermentation and its maintenance throughout the glucose-limiting fed-batch phase led to a nearly 3-fold increase of product yield, to 14.6%. The novelB. subtilisself-induction system thus makes a considerable contribution to improving product yield and reducing the costs associated with its technical application.

scholarly journals Optimized polymer-based glucose release in microtiter plates for small-scale E. coli fed-batch cultivations

2020 ◽  
Vol 14 (1) ◽  
Author(s):  
Timm Keil ◽  
Barbara Dittrich ◽  
Clemens Lattermann ◽  
Jochen Büchs
Keyword(s):  
Release Rate ◽  
Oxygen Transfer ◽  
Oxygen Transfer Rate ◽  
Small Scale ◽  
Fed Batch ◽  
Release Rates ◽  
Glucose Release ◽  
E Coli ◽  
Batch Phase ◽  
Microtiter Plates

Abstract Background Small-scale cultivation vessels, which allow fed-batch operation mode, become more and more important for fast and reliable early process development. Recently, the polymer-based feeding system was introduced to allow fed-batch conditions in microtiter plates. Maximum glucose release rates of 0.35 mg/h per well (48-well-plate) at 37 °C can be achieved with these plates, depending on the media properties. The fed-batch cultivation of fluorescent protein-expressing E. coli at oxygen transfer rate levels of 5 mmol/L/h proved to be superior compared to simple batch cultivations. However, literature suggests that higher glucose release rates than achieved with the currently available fed-batch microtiter plate are beneficial, especially for fast-growing microorganisms. During the fed-batch phase of the cultivation, a resulting oxygen transfer rate level of 28 mmol/L/h should be achieved. Results Customization of the polymer matrix enabled a considerable increase in the glucose release rate of more than 250% to up to 0.90 mg/h per well. Therefore, the molecular weight of the prepolymer and the addition of a hydrophilic PDMS-PEG copolymer allowed for the individual adjustment of a targeted glucose release rate. The newly developed polymer matrix was additionally invariant to medium properties like the osmotic concentration or the pH-value. The glucose release rate of the optimized matrix was constant in various synthetic and complex media. Fed-batch cultivations of E. coli in microtiter plates with the optimized matrix revealed elevated oxygen transfer rates during the fed-batch phase of approximately 28 mmol/L/h. However, these increased glucose release rates resulted in a prolonged initial batch phase and oxygen limitations. The newly developed polymer-based feeding system provides options to manufacture individual feed rates in a range from 0.24–0.90 mg/h per well. Conclusions The optimized polymer-based fed-batch microtiter plate allows higher reproducibility of fed-batch experiments since cultivation media properties have almost no influence on the release rate. The adjustment of individual feeding rates in a wide range supports the early process development for slow, average and fast-growing microorganisms in microtiter plates. The study underlines the importance of a detailed understanding of the metabolic behavior (through online monitoring techniques) to identify optimal feed rates.

Simulation of UDMC on a Fed-Batch Bioreactor

1988 ◽  
Author(s):  
Hsin-Ying Lin ◽  
John C. Lewis ◽  
Richard H. Luecke
Keyword(s):  
Fed Batch ◽  
Batch Bioreactor

Glycerol Synthesis Attenuation ofCandida glycerinogenesin Fed-batch Fermentation

2012 ◽  
Vol 18 (5) ◽  
pp. 791
Author(s):  
Xiaoyun DING ◽  
Bin ZHUGE ◽  
Huiying FANG ◽  
Hong ZONG ◽  
Xiaoxiao LIU ◽  
...  
Keyword(s):  
Batch Fermentation ◽  
Fed Batch ◽  
Fed Batch Fermentation ◽  
Glycerol Synthesis
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