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A rate-based combined heat and mass transfer model developed based on penetration theory is used to study the effect of water evaporation and condensation on the CO2 absorption process using six different cases with real pilot-scale plants flue gas conditions.
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For the heat transfer coefficient a model based on the penetration theory is used.
A model based on the penetration theory was used to analyze the experimental data and to determine the kinetic rate constant for the reaction between COS and MDEA.
These estimates were found to lie more in line with experimental results in literature than previously used mass transfer models based on Higbie׳s penetration theory.
A model based on the penetration theory has been developed to calculate the dynamic absorption rate of sulfur dioxide into a droplet of limestone slurry.
A phenomenological model of mass transfer and chemical reaction, based on the penetration theory, is employed to simulate the interfacial phenomena in gas liquid reactors, and a study of CO2 absorption into alkali solution is presented to demonstrate the method.
It is based on Higbie's penetration theory and Kolmogoroff's theory of isotropic turbulence.
A theoretical equation based on Hibie's penetration theory and the isotropic turbulence theory of Kolmogoroff is used for kL determination.
The description is based on the Higbie penetration theory.
A coupled mass transfer-kinetics-equilibrium mathematical model based on Higbie's penetration theory has been developed with the assumption that all reactions are reversible.
The results of the present approximation were for various reactions compared to the numerical enhancement factors obtained for the model based on the Higbie penetration theory.
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