In the present work, the process of carbon dioxide absorption is analyzed at high partial pressures, in aqueous solutions of 1-amino-2-propanol (monoisopropanolamine (MIPA)), in relation to the thermal effects involved. All experiments were made in a stirred-tank reactor with a plane unbroken gas−liquid interface. The variables considered were the MIPA concentration within the range 0.1−2.0 M and the temperature within the interval 288−308 K. From the results, we deduce that the absorption process takes place in the nonisothermal instantaneous regime and propose an equation which not only relates the experimental results of flow density with the initial concentration of amine but at the same time enables the evaluation of the rise in temperature in the gas−liquid interface.
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Camacho et al. (1997) studied this question.
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