TY - GEN
T1 - A thermodynamic robust model to assess hybrid solvents for CO2 capture
AU - Alkhatib, Ismail
AU - Al-Hajaj, Ahmed
AU - Abu Zahra, Mohammad
AU - Vega, Lourdes
N1 - Funding Information:
Financial support for this work has been provided by Khalifa University of Science and Technology under project RC2-2019-007. Additional funding was provided by ADNOC Gas Processing and their stakeholders Shell, Total and Partex, under the Gas Research Center (project GRC2018-003). Resources from the Computational laboratory of the RICH Center are also gratefully acknowledged.
Publisher Copyright:
© 2020, Society of Petroleum Engineers
PY - 2020
Y1 - 2020
N2 - The molecular-based soft-SAFT equation of state has been applied to describe the chemisorption of CO2 in non-aqueous hybrid solvents of mixtures of AMP and glycols. The reactive nature of the CO2 absorption process in non-aqueous amines was implicitly modelled by the formation of CO2-amine physical aggregates bounded by strong and localised intermolecular interactions. This modelling framework only required VLE data on the absorption of CO2 in amine solvents, without the need for additional information such as speciation reactions or equilibrium constants. Subsequently, the developed models were used to examine the CO2 capture performance of these hybrid solvents in terms of absorption cyclic capacity and heat of regeneration as key performance indicators using a simple and short-cut estimation method. Results show that for the same total amine mass concentration, non-aqueous AMP solvents possess a 30-40% decrease in total heat of regeneration compared to their aqueous counterparts at the expense of a 20-50% reduction in cyclic capacity. These results validate the reliability of the molecular modelling approach as an attractive and valuable tool for the screening of chemical solvents and process modelling.
AB - The molecular-based soft-SAFT equation of state has been applied to describe the chemisorption of CO2 in non-aqueous hybrid solvents of mixtures of AMP and glycols. The reactive nature of the CO2 absorption process in non-aqueous amines was implicitly modelled by the formation of CO2-amine physical aggregates bounded by strong and localised intermolecular interactions. This modelling framework only required VLE data on the absorption of CO2 in amine solvents, without the need for additional information such as speciation reactions or equilibrium constants. Subsequently, the developed models were used to examine the CO2 capture performance of these hybrid solvents in terms of absorption cyclic capacity and heat of regeneration as key performance indicators using a simple and short-cut estimation method. Results show that for the same total amine mass concentration, non-aqueous AMP solvents possess a 30-40% decrease in total heat of regeneration compared to their aqueous counterparts at the expense of a 20-50% reduction in cyclic capacity. These results validate the reliability of the molecular modelling approach as an attractive and valuable tool for the screening of chemical solvents and process modelling.
UR - http://www.scopus.com/inward/record.url?scp=85097537859&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:85097537859
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 -