Solubility of CO2 in 15, 30, 45 and 60 mass% MEA from 40 to 120°C and model representation using the extended UNIQUAC framework

Chemical Engineering Science

Volumn 66, Issue 24, 2011, Pages 6393-6406

  Aronu, Ugochukwu E ^a   Gondal, Shahla ^a   Hessen, Erik T ^a   Haug Warberg, Tore ^a   Hartono, Ardi ^a   Hoff, Karl A ^b   Svendsen, Hallvard F ^a  

^a NORWEGIAN UNIVERSITY OF SCIENCE AND TECHNOLOGY   (Norway)

^b SINTEF MATERIALS AND CHEMISTRY   (Norway)

Author keywords

CO2 absorption; Extended UNIQUAC; Monoethanolamine (MEA); Phase equilibria; Separations; Thermodynamic process

Indexed keywords

AVERAGE ABSOLUTE RELATIVE DEVIATIONS; EQUILIBRIUM APPARATUS; EXCESS ENTHALPIES; EXPERIMENTAL DATA; FREEZING-POINT DEPRESSION; HIGH TEMPERATURE; LIQUID PHASE; LITERATURE DATA; LOW TEMPERATURE EQUILIBRIUM; MODEL PARAMETERS; MODEL REPRESENTATION; MONOETHANOLAMINE; PHYSICAL SOLUBILITY; SOLUBILITY DATA; THERMODYNAMIC PROCESS; TOTAL PRESSURE; UNIQUAC; UNIQUAC MODELS; VAPOR-LIQUID EQUILIBRIUM; VLE DATA;

LIQUIDS; PARTIAL PRESSURE; PHASE EQUILIBRIA; SOLUBILITY; TEMPERATURE;

CARBON DIOXIDE;

EID: 80054915748     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2011.08.042     Document Type: Article

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