Average shear rate for non-Newtonian fluids in a concentric-tube airlift bioreactor

Author:

Cerri M.O.,Futiwaki L.,Jesus C.D.F.,Cruz A.J.G.,Badino A.C.

Publisher

Elsevier BV

Subject

Biomedical Engineering,Environmental Engineering,Bioengineering,Biotechnology

Reference30 articles.

1. Airlift Bioreactors;Chisti,1989

2. Airlift fermenters: construction, behavior, and uses;Onken;Adv. Biotechnol. Processes,1983

3. Mathematical models for design of bioreactors: applications of Kolmogoroff's theory of isotropic turbulence;Kawase;Chem. Eng. J.,1990

4. Mixing and mass transfer in concentric-tube airlift fermenters: Newtonian and non-Newtonian media;Kawase;J. Chem. Technol. Biotechnol.,1986

5. Theoretical prediction of volumetric mass transfer coefficients in bubble columns for Newtonian and non-Newtonian fluids;Kawase;Chem. Eng. Sci.,1987

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