Local Distribution of Oxygen Mass Transfer Coefficient in CMC Solutions in Bioreactors Furnished with Different Types of Coaxial Mixers
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[1] A. Lohi,et al. Analysis of power consumption for gas dispersion in non-Newtonian fluids with a coaxial mixer: New correlations for Reynolds and power numbers , 2020, Chemical Engineering Journal.
[2] A. Lohi,et al. Experimental Analysis of the Mass Transfer Coefficient and Interfacial Area in an Aerated Coaxial Mixing System Comprising a Non-Newtonian Solution , 2020 .
[3] A. Lohi,et al. Local and overall gas holdup in an aerated coaxial mixing system containing a non‐ Newtonian fluid , 2020 .
[4] S. Jegatheeswaran,et al. Use of Gas Helicity as an Indicator to Evaluate Impeller Design and its Gas Holdup: Proof of Concept for the Intensification of Gas-Liquid Mixing , 2020 .
[5] A. Lohi,et al. Intensification of gas dispersion in pseudoplastic fluids with coaxial mixers , 2020 .
[6] S. Jegatheeswaran,et al. Investigation of the detrimental effect of the rotational speed on gas holdup in non-Newtonian fluids with Scaba-anchor coaxial mixer: A paradigm shift in gas-liquid mixing , 2020 .
[7] Md. Tariqul Islam,et al. Single bubble rising behaviors in Newtonian and non‐Newtonian fluids with validation of empirical correlations: A computational fluid dynamics study , 2020, Engineering Reports.
[8] S. Jegatheeswaran,et al. Enhanced aeration efficiency in non-Newtonian fluids using coaxial mixers: High-solidity ratio central impeller with an anchor , 2019 .
[9] P. Ouyang,et al. Hydrodynamics, mass transfer and cell growth characteristics in a novel microbubble stirred bioreactor employing sintered porous metal plate impeller as gas sparger , 2018, Chemical Engineering Science.
[10] M. Nasr,et al. Analysis of gas holdup and bubble behavior in a biopolymer solution inside a bioreactor using tomography and dynamic gas disengagement techniques , 2018 .
[11] Farhad Ein-Mozaffari,et al. Hydrodynamic characteristics of an aerated coaxial mixing vessel equipped with a pitched blade turbine and an anchor , 2018 .
[12] A. Lohi,et al. Effect of Impeller Spacing on the Flow Field of Yield-Pseudoplastic Fluids Generated by a Coaxial Mixing System Composed of Two Central Impellers and an Anchor , 2017 .
[13] A. J. Cruz,et al. Influence of dual-impeller type and configuration on oxygen transfer, power consumption, and shear rate in a stirred tank bioreactor , 2016 .
[14] D. K. Hwang,et al. Analysis of power consumption and gas holdup distribution for an aerated reactor equipped with a coaxial mixer: Novel correlations for the gas flow number and gassed power , 2016 .
[15] Leila Pakzad,et al. Investigation of hydrodynamic performances of coaxial mixers in agitation of yield-pseudoplasitc fluids: Single and double central impellers in combination with the anchor , 2016 .
[16] D. K. Hwang,et al. Analysis of mixing in an aerated reactor equipped with the coaxial mixer through electrical resistance tomography and response surface method , 2016 .
[17] D. K. Hwang,et al. Experimental investigation of the bubble behavior in an aerated coaxial mixing vessel through electrical resistance tomography (ERT) , 2016 .
[18] Ju Chu,et al. Flow Pattern, Mixing, Gas Hold-Up and Mass Transfer Coefficient of Triple-Impeller Configurations in Stirred Tank Bioreactors , 2014 .
[19] H. Noorman,et al. Power consumption, local and average volumetric mass transfer coefficient in multiple-impeller stirred bioreactors for xanthan gum solutions , 2014 .
[20] Heath Rushing,et al. Design and Analysis of Experiments by Douglas Montgomery: A Supplement for Using JMP , 2013 .
[21] Maritza Catalina Condori Bustamante,et al. Comparison between average shear rates in conventional bioreactor with Rushton and Elephant ear impellers , 2013 .
[22] J. Morchain,et al. Effect of Tank Size on k L a and Mixing Time in Aerated Stirred Reactors With Non-Newtonian Fluids , 2011 .
[23] Miguel A. Galán,et al. Mass transfer rates from bubbles in stirred tanks operating with viscous fluids , 2010 .
[24] A. Brucato,et al. Simplified dynamic pressure method for kLa measurement in aerated bioreactors , 2010 .
[25] Ning Chen,et al. Fluid dynamics investigation of variant impeller combinations by simulation and fermentation experiment , 2009 .
[26] F. García-Ochoa,et al. Bioreactor scale-up and oxygen transfer rate in microbial processes: an overview. , 2009, Biotechnology advances.
[27] Václav Linek,et al. Improved power and mass transfer correlations for design and scale-up of multi-impeller gas–liquid contactors , 2009 .
[28] Václav Linek,et al. Mass transfer correlations for multiple-impeller gas–liquid contactors. Analysis of the effect of axial dispersion in gas and liquid phases on “local”kLa values measured by the dynamic pressure method in individual stages of the vessel , 2007 .
[29] Vivek V. Ranade,et al. CFD simulation of mixing in tall gas-liquid stirred vessel: Role of local flow patterns , 2006 .
[30] Aniruddha B. Pandit,et al. Gas–liquid mass transfer studies with triple impeller system on a laboratory scale bioreactor , 2005 .
[31] Václav Linek,et al. Gas–liquid mass transfer coefficient in stirred tanks interpreted through models of idealized eddy structure of turbulence in the bubble vicinity , 2004 .
[32] Jorge M. T. Vasconcelos,et al. Gas-liquid mass transfer coefficient in stirred tanks interpreted through bubble contamination kinetics , 2004 .
[33] S. Rhee,et al. Impeller types and feeding modes influence the morphology and protein expression in the submerged culture ofAspergillus oryzae , 2004 .
[34] Felix Garcia-Ochoa,et al. Theoretical Prediction of Gas-Liquid Mass Transfer Coefficient, Specific Area and Hold-Up in Sparged Stirred Tanks , 2004 .
[35] Václav Linek,et al. Gas hold-up, mixing time and gas-liquid volumetric mass transfer coefficient of various multiple-impeller configurations: Rushton turbine, pitched blade and techmix impeller and their combinations , 2003 .
[36] Mamoru Ishii,et al. Interfacial area concentration of bubbly flow systems , 2002 .
[37] Jpk Seville,et al. Fluid trajectories in a stirred vessel of non-newtonian liquid using positron emission particle tracking , 2000 .
[38] Alvin W. Nienow,et al. Mixing in large-scale vessels stirred with multiple radial or radial and axial up-pumping impellers: modelling and measurements , 2000 .
[39] Gogate,et al. Multiple-impeller systems with a special emphasis on bioreactors: a critical review. , 2000, Biochemical engineering journal.
[40] Peter Vrábel,et al. Compartment Model Approach: Mixing in Large Scale Aerated Reactors with Multiple Impellers , 1999 .
[41] A. Nienow,et al. Dependence of penicillium chrysogenum growth, morphology, vacuolation, and productivity in fed-batch fermentations on impeller type and agitation intensity , 1998, Biotechnology and bioengineering.
[42] Michel Roustan,et al. Bubble size and mass transfer coefficients in dual‐impeller agitated reactors , 1998 .
[43] S. J. Arjunwadkar,et al. Gas-liquid mass transfer in dual impeller bioreactor , 1998 .
[44] V. Linek,et al. Gas-liquid mass transfer in vessels stirred with multiple impellers—II. Modelling of gas-liquid mass transfer , 1996 .
[45] Jaya Narayan Sahu,et al. Effect of interfacial forces and turbulence models on predicting flow pattern inside the bubble column , 2014 .
[46] J. Chu,et al. Effects of flow field on the metabolic characteristics of Streptomyces lincolnensis in the industrial fermentation of lincomycin. , 2013, Journal of bioscience and bioengineering.
[47] Gao Xiong-hou. Power Demand and Mixing Performance of Coaxial Mixers in Newtonian Liquids , 2010 .
[48] S. S. Alves,et al. Effect of blade shape on the performance of six-bladed disk turbine impellers , 2000 .
[49] M. Gavrilescu,et al. The volumetric oxygen mass transfer coefficient in antibiotic biosynthesis liquids , 1993 .
[50] M. F. Edwards,et al. Mixing in the process industries , 1985 .