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Theoretical prediction of the mass transfer coefficients in bubble columns operating in churn-turbulent flow regime. Study in Newtonian and non-Newtonian fluids under different operation conditions
Study in Newtonian and non-Newtonian fluids under different operation ... transfer coefficients in bubble columns operating in churn-turbulent flow regime.
E Alvarez 著2001被引用数: 6 — Theoretical prediction of the mass transfer coefficients in bubble columns operating in churn-turbulent flow regime. Study in Newtonian and non-Newtonian fluids ...
Theoretical prediction of the mass transfer coefficients in bubble columns operating in churn-turbulent flow regime. Study in Newtonian and non-Newtonian fluids ...
It was found that in the gas-liquid bubble column (0.095 m in ID) the modified ... properties on mass transfer in bubble columns with non-Newtonian fluids.
Theoretical prediction of the mass transfer coefficients in bubble ... L a with Newtonian and non-Newtonian fluids in bubble columns using CO2 as gas phase ...
N Kantarci 著2005被引用数: 940 — Keywords: Bubble columns; Bioreactors; Gas holdup; Heat transfer; Mass transfer; ... observed the churn-turbulent flow regime for gas superficial.
A Fallahi 著2019 — The developed correlation for predicting the mass transfer ... Figure 2.4- Flow regime diagram in bubble columns depending on gas velocity and column.
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L Li 著2021 — diameter of bubble column. h. heat transfer coefficient, kW·(m2·K)–1. kL. the liquid-side mass transfer coefficient.
Column diameter is larger than 150 mm, which means the bubble column operates in the bubble flow regime (highly viscous liquid phase or non-Newtonian ...
G Besagni 著被引用数: 86 — The main processes involved in the reactive mass transfer phenomena. 2. Bubble Column Fluid-Dynamics. In this section, the flow regimes, flow regime ...

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