TY - GEN
T1 - Assessing the feasibility of deep eutectic solvents for CO2 capture from molecular and process modeling
AU - Alkhatib, Ismail
AU - Alba, Carlos
AU - Bahamon, Daniel
AU - Llovell, Felix
AU - Vega, Lourdes
N1 - Funding Information:
Financial support for this work has been provided by Khalifa University under project RC2-2019-007. Additional funding has been provided by project PID2019-108014RB-C21 supported by the Spanish Ministry of Science and Innovation.
Publisher Copyright:
© 2020, Society of Petroleum Engineers
PY - 2020
Y1 - 2020
N2 - The soft-SAFT equation of state is employed for the screening of deep eutectic solvents (DES) for CO2 capture based on key performance indicators, namely, CO2 absorption capacity, and enthalpy of absorption. This work belongs to a long-term project on assessing the adequacy of advanced EoSs (soft-SAFT) as a tool for the evaluation and design of alternative solvents for CO2 capture. The models for the pure DESs and their mixtures with CO2 are validated with experimental data, and subsequently used in a fully predictive manner to calculate the thermophysical properties needed for evaluating solvent performance. Results demonstrate that under the same operating conditions, [TBA] [Cl]:LA (1:2) is the most promising DES in terms of amount of CO2 absorbed and enthalpy of absorption. However, the comparison of these solvents to 30 wt.% aqueous MDEA solution shows that the promise of DESs is far from adequate in terms of CO2 solubility, being 13 times lower than that obtained with aqueous MDEA. Nevertheless, DESs show a clear advantage in terms of lower enthalpy of absorption, being 3 times less than aqueous MDEA, along with the absence of water as a co-solvent. The collection of the acquired results confirms the reliability of the soft-SAFT EoS as an attractive and valuable screening tool for CO2 capture and process modelling.
AB - The soft-SAFT equation of state is employed for the screening of deep eutectic solvents (DES) for CO2 capture based on key performance indicators, namely, CO2 absorption capacity, and enthalpy of absorption. This work belongs to a long-term project on assessing the adequacy of advanced EoSs (soft-SAFT) as a tool for the evaluation and design of alternative solvents for CO2 capture. The models for the pure DESs and their mixtures with CO2 are validated with experimental data, and subsequently used in a fully predictive manner to calculate the thermophysical properties needed for evaluating solvent performance. Results demonstrate that under the same operating conditions, [TBA] [Cl]:LA (1:2) is the most promising DES in terms of amount of CO2 absorbed and enthalpy of absorption. However, the comparison of these solvents to 30 wt.% aqueous MDEA solution shows that the promise of DESs is far from adequate in terms of CO2 solubility, being 13 times lower than that obtained with aqueous MDEA. Nevertheless, DESs show a clear advantage in terms of lower enthalpy of absorption, being 3 times less than aqueous MDEA, along with the absence of water as a co-solvent. The collection of the acquired results confirms the reliability of the soft-SAFT EoS as an attractive and valuable screening tool for CO2 capture and process modelling.
UR - http://www.scopus.com/inward/record.url?scp=85097526522&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:85097526522
T3 - Society of Petroleum Engineers - Abu Dhabi International Petroleum Exhibition and Conference 2020, ADIP 2020
BT - Society of Petroleum Engineers - Abu Dhabi International Petroleum Exhibition and Conference 2020, ADIP 2020
T2 - Abu Dhabi International Petroleum Exhibition and Conference 2020, ADIP 2020
Y2 - 9 November 2020 through 12 November 2020
ER -