TY - JOUR
T1 - A hybrid equation of state and Kent-Eisenberg model for accurate prediction of carbon dioxide separation by aqueous alkanolamines
AU - Suleman, Humbul
AU - Maulud, Abdulhalim Shah
AU - Man, Zakaria
PY - 2016/11/21
Y1 - 2016/11/21
N2 - A hybrid predictive model has been developed for accurate prediction of thermodynamics of carbon dioxide separation by aqueous alkanolamines. The model incorporates equation of state/excess Gibbs energy model into Kent–Eisenberg approach to predict carbon dioxide–alkanolamine–water equilibria. The approach imparts theoretical corrections to Kent–Eisenberg approach and significantly extends their range of application for monoethanolamine, diethanolamine, methyldiethanolamine, and 2-amino-2-methyl-1-propanol solutions. The proposed model suitably predicts thermodynamics of carbon dioxide separation, well beyond the regressed range of parameters. The results are in excellent agreement with experimental data for a wide range of process parameters and found superior to existing thermodynamic approaches.
AB - A hybrid predictive model has been developed for accurate prediction of thermodynamics of carbon dioxide separation by aqueous alkanolamines. The model incorporates equation of state/excess Gibbs energy model into Kent–Eisenberg approach to predict carbon dioxide–alkanolamine–water equilibria. The approach imparts theoretical corrections to Kent–Eisenberg approach and significantly extends their range of application for monoethanolamine, diethanolamine, methyldiethanolamine, and 2-amino-2-methyl-1-propanol solutions. The proposed model suitably predicts thermodynamics of carbon dioxide separation, well beyond the regressed range of parameters. The results are in excellent agreement with experimental data for a wide range of process parameters and found superior to existing thermodynamic approaches.
UR - http://dx.doi.org/10.1080/01496395.2016.1217241
U2 - 10.1080/01496395.2016.1217241
DO - 10.1080/01496395.2016.1217241
M3 - Article
SN - 0149-6395
VL - 51
SP - 2744
EP - 2755
JO - Separation Science and Technology
JF - Separation Science and Technology
IS - 17
ER -