2020
DOI: 10.1016/j.tibtech.2020.01.009
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Developing a Computational Framework To Advance Bioprocess Scale-Up

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Cited by 60 publications
(33 citation statements)
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“…The scale-up of bioreactors and biotechnological processes is a critical operation in industrial biotechnology. In many cases, due to limitations in the applied methodology, a scale-up results in reduced titers, yields or productivities [147] . For the layout and design of bioreactors, mainly of the stirred tank type, there was a strong focus on the numerical simulation and analysis of local effects in the 1980's [148] , [149] , [150] .…”
Section: Current Research and Future Trendsmentioning
confidence: 99%
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“…The scale-up of bioreactors and biotechnological processes is a critical operation in industrial biotechnology. In many cases, due to limitations in the applied methodology, a scale-up results in reduced titers, yields or productivities [147] . For the layout and design of bioreactors, mainly of the stirred tank type, there was a strong focus on the numerical simulation and analysis of local effects in the 1980's [148] , [149] , [150] .…”
Section: Current Research and Future Trendsmentioning
confidence: 99%
“…The application of these approaches in real-time is nowadays still restricted to comparably simple systems at lower resolutions, as merging CFD and dynamic models for microbially catalyzed reactions is accompanied by a high demand of processing power. In the future, these integrated approaches are a promising trend for a truly knowledge-based bioreactor scale-up and layout [147] . Eventually, once real-time operation is made feasible, this approach can be advanced to a framework for online control of bioprocesses.…”
Section: Current Research and Future Trendsmentioning
confidence: 99%
“…Although the interplay between cell systems and their production conditions can be measured, the underlying mechanism is partially unknown, which is, however, seldom accounted for during lab-scale research and development [3,4]. Representatively, the nonideal mixing and mass transfer limitations at the large scale in most cases are not rigorously considered in lab-scale designs, and thus the outcome of the environmental impacts cannot match the reality at the large scale [5,6]. In industrial settings, the environmental gradients, such as those of substrate, dissolved oxygen and pH, caused by insufficient mixing and mass transfer restrictions, and of the shear force caused by the impellers, often exert a negative impact on the resulting commercial indicators (i.e., titer, yield and productivity) and thus the economic benefits [7][8][9].…”
Section: Introductionmentioning
confidence: 99%
“…To calculate the load bearing capacity and failure probability of corroded RC members, the calculation of the minimum cross-sectional area is of vital importance. To meet the convenience of engineers, the indicator R was adopted to determine directly the minimum crosssectional area, regardless of complicated corrosion topography of the rebar [9,10]. Statistical analysis found that the indicator R of corroded rebar can be characterized by Gumbel distribution and both the location parameter and the scale parameter increased linearly with increase in the corrosion degree [10].…”
Section: Introductionmentioning
confidence: 99%