TY - JOUR
T1 - A Robust Framework for Generating Adsorption Isotherms to Screen Materials for Carbon Capture
AU - Moubarak, Elias
AU - Moosavi, Seyed Mohamad
AU - Charalambous, Charithea
AU - Garcia, Susana
AU - Smit, Berend
N1 - Funding Information:
This work is part of the PrISMa Project (299659), funded through the ACT Programme (Accelerating CCS Technologies, Horizon 2020 Project 294766). Financial contributions from the Department for Business, Energy & Industrial Strategy (BEIS), together with extra funding from the NERC and EPSRC Research Councils, United Kingdom, the Research Council of Norway (RCN), the Swiss Federal Office of Energy (SFOE), and the U.S. Department of Energy, are gratefully acknowledged. Additional financial support from TOTAL and Equinor is also gratefully acknowledged. C.C. and S.G. are also supported by the UKRI ISCF Industrial Challenge within the U.K. Industrial Decarbonisation Research and Innovation Centre (IDRIC) Award No. EP/V027050/1. S.M.M. acknowledges support from the Swiss National Science Foundation (SNSF) under Grant P2ELP2_195155.
Publisher Copyright:
© 2023 The Authors. Published by American Chemical Society.
PY - 2023/7/5
Y1 - 2023/7/5
N2 - To rank the performance of materials for a given carbon
capture process, we rely on pure component isotherms from which we predict the
mixture isotherms. For screening a large number of materials, we also
increasingly rely on isotherms predicted from molecular simulations. In
particular, for such screening studies, it is important that the procedures to
generate the data are accurate, reliable, and robust. In this work, we develop
an efficient and automated workflow for a meticulous sampling of pure component
isotherms. The workflow was tested on a set of metal–organic frameworks (MOFs)
and proved to be reliable given different guest molecules. We show that the
coupling of our workflow with the Clausius–Clapeyron relation saves CPU time,
yet enables us to accurately predict pure component isotherms at the
temperatures of interest, starting from a reference isotherm at a given
temperature. We also show that one can accurately predict the CO2 and
N2 mixture isotherms using ideal adsorbed solution theory
(IAST). In particular, we show that IAST is a more reliable numerical tool to
predict binary adsorption uptakes for a range of pressures, temperatures, and
compositions, as it does not rely on the fitting of experimental data, which
typically needs to be done with analytical models such as dual-site Langmuir
(DSL). This makes IAST a more suitable and general technique to bridge the gap
between adsorption (raw) data and process modeling. To demonstrate this point,
we show that the ranking of materials, for a standard three-step temperature
swing adsorption (TSA) process, can be significantly different depending on the
thermodynamic method used to predict binary adsorption data. We show that, for
the design of processes that capture CO2 from low concentration
(0.4%) streams, the commonly used methodology to predict mixture isotherms
incorrectly assigns up to 33% of the materials as top-performing.
AB - To rank the performance of materials for a given carbon
capture process, we rely on pure component isotherms from which we predict the
mixture isotherms. For screening a large number of materials, we also
increasingly rely on isotherms predicted from molecular simulations. In
particular, for such screening studies, it is important that the procedures to
generate the data are accurate, reliable, and robust. In this work, we develop
an efficient and automated workflow for a meticulous sampling of pure component
isotherms. The workflow was tested on a set of metal–organic frameworks (MOFs)
and proved to be reliable given different guest molecules. We show that the
coupling of our workflow with the Clausius–Clapeyron relation saves CPU time,
yet enables us to accurately predict pure component isotherms at the
temperatures of interest, starting from a reference isotherm at a given
temperature. We also show that one can accurately predict the CO2 and
N2 mixture isotherms using ideal adsorbed solution theory
(IAST). In particular, we show that IAST is a more reliable numerical tool to
predict binary adsorption uptakes for a range of pressures, temperatures, and
compositions, as it does not rely on the fitting of experimental data, which
typically needs to be done with analytical models such as dual-site Langmuir
(DSL). This makes IAST a more suitable and general technique to bridge the gap
between adsorption (raw) data and process modeling. To demonstrate this point,
we show that the ranking of materials, for a standard three-step temperature
swing adsorption (TSA) process, can be significantly different depending on the
thermodynamic method used to predict binary adsorption data. We show that, for
the design of processes that capture CO2 from low concentration
(0.4%) streams, the commonly used methodology to predict mixture isotherms
incorrectly assigns up to 33% of the materials as top-performing.
KW - Industrial and Manufacturing Engineering
KW - General Chemical Engineering
KW - General Chemistry
UR - http://www.scopus.com/inward/record.url?scp=85164433507&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.3c01358
DO - 10.1021/acs.iecr.3c01358
M3 - Article
C2 - 37425135
SN - 0888-5885
VL - 62
SP - 10252
EP - 10265
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 26
ER -