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Synergistically applying 1-D modeling and CFD for designing industrial scale bubble column syngas bioreactors.


ABSTRACT: The reduction of greenhouse gas emissions and future perspectives of circular economy ask for new solutions to produce commodities and fine chemicals. Large-scale bubble columns operated by gaseous substrates such as CO, CO2, and H2 to feed acetogens for product formations could be promising approaches. Valid in silico predictions of large-scale performance are needed to dimension bioreactors properly taking into account biological constraints, too. This contribution deals with the trade-off between sophisticated spatiotemporally resolved large-scale simulations using computationally intensive Euler-Euler and Euler-Lagrange approaches and coarse-grained 1-D models enabling fast performance evaluations. It is shown that proper consideration of gas hold-up is key to predict biological performance. Intrinsic bias of 1-D models can be compensated by reconsideration of Sauter diameters derived from uniquely performed Euler-Lagrange computational fluid dynamics.

SUBMITTER: Siebler F 

PROVIDER: S-EPMC7336164 | biostudies-literature | 2020 Jul

REPOSITORIES: biostudies-literature

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Synergistically applying 1-D modeling and CFD for designing industrial scale bubble column syngas bioreactors.

Siebler Flora F   Lapin Alexey A   Takors Ralf R  

Engineering in life sciences 20200213 7


The reduction of greenhouse gas emissions and future perspectives of circular economy ask for new solutions to produce commodities and fine chemicals. Large-scale bubble columns operated by gaseous substrates such as CO, CO<sub>2</sub>, and H<sub>2</sub> to feed acetogens for product formations could be promising approaches. Valid in silico predictions of large-scale performance are needed to dimension bioreactors properly taking into account biological constraints, too. This contribution deals  ...[more]

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