The influence of the configurations of multiple-impeller on canrenone bioconversion using resting cells of Aspergillus ochraceus
Author:
Affiliation:
1. Department of Biological Engineering , Shanghai Institute of Technology , Shanghai 201418 , P.R. China
2. Department of Biological Engineering , East China University of Science and Technology , Shanghai 200237 , P.R. China
Abstract
Publisher
Walter de Gruyter GmbH
Subject
General Chemical Engineering
Link
https://www.degruyter.com/document/doi/10.1515/ijcre-2022-0219/pdf
Reference35 articles.
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2. Azargoshasb, H., S. M. Mousavi, O. Jamialahmadi, S. A. Shojaosadati, and S. B. Mousavi. 2016. “Experiments and a Three‐Phase Computational Fluid Dynamics (CFD) Simulation Coupled with Population Balance Equations of a Stirred Tank Bioreactor for High Cell Density Cultivation.” Canadian Journal of Chemical Engineering 94 (1): 20–32. https://doi.org/10.1002/cjce.22352.
3. Babalona, E., D. Bahouma, S. Tagia, E. Pantouflas, and J. Markopoulos. 2005. “Power Consumption in Dual Impeller Gas‐Liquid Contactors: Impeller Spacing, Gas Flow Rate, and Viscosity Effects.” Chemical Engineering & Technology 28 (7): 802–7. https://doi.org/10.1002/ceat.200407160.
4. Bao, Y., Z. Hao, Z. Gao, L. Shi, and J. M. Smith. 2004. “Suspension of Buoyant Particles in a Three Phase Stirred Tank.” Chemical Engineering Science 60 (8): 2283–92. https://doi.org/10.1016/j.ces.2004.10.040.
5. Böhm, L., L. Hohl, C. Bliatsiou, and M. Kraume. 2019. “Multiphase Stirred Tank Bioreactors-New Geometrical Concepts and Scale‐up Approaches.” Chemie Ingenieur Technik 91 (12): 1724–46. https://doi.org/10.1002/cite.201900165.
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