TY - JOUR
T1 - Evaluation of the protic ionic liquid, N,N-dimethyl-aminoethylammonium formate for CO2 capture
AU - Mumford, Kathryn
AU - Pas, Steven James
AU - Linseisen, Thomas
AU - Statham, Tom M
AU - Nicholas, Nathan Johann
AU - Lee, Sangyun
AU - Kezia, Kezia
AU - Ranganathan, Vijayaraghavan
AU - Macfarlane, Douglas Robert
AU - Stevens, Geoffrey W
PY - 2015
Y1 - 2015
N2 - A protic ionic ethylenediamine liquid N,N-dimethyl-aminoethylammonium formate (DMEDAH formate) was evaluated for the removal of carbon dioxide from carbon dioxide and nitrogen mixed gas streams. This evaluation was conducted via a series of vapour-liquid equilibrium (VLE) experiments, wetted wall measurements and solvent contactor trials with the results compared to the performance of the industrial standard 30wt monoethanolamine (MEA). The VLE of the ionic liquid indicated that the sorption process included a chemical reaction component and is comparable to MEA. The mass transfer coefficient, calculated via the wetted wall column apparatus is an order of magnitude lower than MEA, which is likely due to the higher viscosity of the ionic liquid and its impact on carbon dioxide diffusivity. The solvent contactor trials indicated the solvent may be used in such an arrangement with good performance at low CO2 loadings, but would benefit from the use of alternative membrane materials.
AB - A protic ionic ethylenediamine liquid N,N-dimethyl-aminoethylammonium formate (DMEDAH formate) was evaluated for the removal of carbon dioxide from carbon dioxide and nitrogen mixed gas streams. This evaluation was conducted via a series of vapour-liquid equilibrium (VLE) experiments, wetted wall measurements and solvent contactor trials with the results compared to the performance of the industrial standard 30wt monoethanolamine (MEA). The VLE of the ionic liquid indicated that the sorption process included a chemical reaction component and is comparable to MEA. The mass transfer coefficient, calculated via the wetted wall column apparatus is an order of magnitude lower than MEA, which is likely due to the higher viscosity of the ionic liquid and its impact on carbon dioxide diffusivity. The solvent contactor trials indicated the solvent may be used in such an arrangement with good performance at low CO2 loadings, but would benefit from the use of alternative membrane materials.
UR - http://goo.gl/IL4n2J
U2 - 10.1016/j.ijggc.2014.11.011
DO - 10.1016/j.ijggc.2014.11.011
M3 - Article
VL - 32
SP - 129
EP - 134
JO - International Journal of Greenhouse Gas Control
JF - International Journal of Greenhouse Gas Control
SN - 1750-5836
ER -