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The document discusses the characteristics of mass transfer between gas-liquid phases in a HiGee reactor, focusing on the absorption process of CO2 using N-methyldiethanolamine (MDEA). It presents a diffusion-reaction mass transfer model that accurately predicts the absorption process under various operational conditions, with experimental results showing good agreement with calculations. The study highlights the importance of liquid film lifetime and dynamic mass transfer coefficients in enhancing mass tra

Author

Roćky Bhaí Haŕsha

Language

EN