TY  - CONF
SN  - 18777058
ID  - scholars7386
Y1  - 2016///
N2  - A thermodynamic framework is presented for determining vapor-liquid equilibrium in carbon dioxide-methyldiethanolamine-water systems. Prediction of vapor-liquid equilibrium has been performed by a modified form of electrolyte-LCVM model. The model incorporates electrolyte NRTL model with translated modified Peng Robinson equation of state by linear combination of Vidal and Michelsen mixing rule. New electrolyte NRTL parameters are reported for the aforementioned system. The predicted results are in good agreement with experimental data and comparable to other thermodynamic approaches, for a wide range of temperature, pressure, methyldiethanolamine concentration and loading values. © 2016 The Authors.
SP  - 902
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-85014046902&doi=10.1016%2fj.proeng.2016.06.498&partnerID=40&md5=e468dfceafd743209de221747dc63b1d
A1  - Suleman, H.
A1  - Maulud, A.S.
A1  - Man, Z.
PB  - Elsevier Ltd
KW  - Alkanolamines; Binary mixtures; Carbon dioxide; Electrolytes; Equations of state; Liquids; Process engineering; Thermodynamics; Waterworks
KW  -  Electrolyte-NRTL model; Linear combinations; Methyldiethanolamine; New electrolytes; Peng-Robinson equation of state; Thermodynamic approaches; Thermodynamic framework; Thermodynamic model
KW  -  Phase equilibria
TI  - Modified e-LCVM EoS/GE Thermodynamic Model for Carbon Dioxide - MDEA - Water System
AV  - none
EP  - 907
VL  - 148
N1  - cited By 3; Conference of 4th International Conference on Process Engineering and Advanced Materials, ICPEAM 2016 ; Conference Date: 15 August 2016 Through 17 August 2016; Conference Code:131138
ER  -