Abstract
AbstractVapor‐liquid equilibrium of CO2 in aqueous mixture of hexamethylenediamine (HMDA) and N‐methyldiethanolamine (MDEA) has been investigated using a stirred equilibrium cell set‐up in the temperature and pressure range of 303–333K and 1–100kPa, respectively. Composition of the mixed amine solvents used are (5mass% HMDA+25mass% MDEA), (10 mass% HMDA+20 mass% MDEA), (15mass% HMDA+15mass% MDEA), and (20 mass% HMDA+10 mass% MDEA). Equilibrium solubility data is fitted using the Kent‐Eisenberg thermodynamic model. To fit experimental solubility data with model predicted data, bicarbamate formation and zwitterion deprotonation reaction equilibrium constants of HMDA are regressed as a function of CO2 loading and temperature. Average absolute deviation between experimental and model predicted data is found to be 7.16%. © 2016 Society of Chemical Industry and John Wiley & Sons, Ltd.
Published Version
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