Process optimization of a fixed bed reactor system for direct air capture
Publication type: Journal Article
Publication date: 2021-09-01
scimago Q1
wos Q2
SJR: 1.486
CiteScore: 10.5
Impact factor: 5.2
ISSN: 17505836, 18780148
Industrial and Manufacturing Engineering
General Energy
Pollution
Management, Monitoring, Policy and Law
Abstract
• Parallel fixed bed reactor system designed for direct air capture by adsorption. • Solid basis for process optimization is achieved through dynamic modelling. • High desorption temperature always desired according to sensitivity analyses. • Weather conditions highly affect direct air capture process performance. The extraction of CO 2 directly from the atmosphere (Direct Air Capture) is commonly employed using supported-amine sorbents. This adsorption technology is under rapid development with novel sorbent materials emerging and with processes being demonstrated on increasingly larger scale. Optimization of such processes requires accurate knowledge on sorbent characteristics and knowledge on how operational variables affect process performance. This study primarily focuses on the latter, where we aim to quantify the influence of operational parameters on the energy duty and CO 2 productivity. In addition, we examine the influence of weather conditions on the adsorption rate. For this, we develop a dynamic model of the complete temperature-vacuum swing adsorption cycle (TVSA). This model was validated by experimental results on a kg-scale direct air capture system. The impact of selected operational variables was assessed by two-dimensional sensitivity analyses. We show that desorption temperature is preferably high, limited by the chemical stability of the sorbent material in this particular case. In addition, the sorbent working capacity should be high when opting for an optimization towards energy duty, whereas it reaches a clear optimum in terms of CO 2 productivity. Finally, we conclude that weather conditions and diurnal variations can significantly affect the performance of a direct air capture process and should certainly be considered during design and operation. With these insights and the developed model, this study provides a sound basis for further process development and optimization of direct air capture using fixed bed technology combined with solid amine sorbents.
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56
Total citations:
56
Citations from 2024:
34
(60.72%)
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Schellevis H. M., Van Schagen T., Brilman D. Process optimization of a fixed bed reactor system for direct air capture // International Journal of Greenhouse Gas Control. 2021. Vol. 110. p. 103431.
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Schellevis H. M., Van Schagen T., Brilman D. Process optimization of a fixed bed reactor system for direct air capture // International Journal of Greenhouse Gas Control. 2021. Vol. 110. p. 103431.
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TY - JOUR
DO - 10.1016/j.ijggc.2021.103431
UR - https://doi.org/10.1016/j.ijggc.2021.103431
TI - Process optimization of a fixed bed reactor system for direct air capture
T2 - International Journal of Greenhouse Gas Control
AU - Schellevis, H M
AU - Van Schagen, Tim
AU - Brilman, D.W.F.
PY - 2021
DA - 2021/09/01
PB - Elsevier
SP - 103431
VL - 110
SN - 1750-5836
SN - 1878-0148
ER -
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BibTex (up to 50 authors)
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@article{2021_Schellevis,
author = {H M Schellevis and Tim Van Schagen and D.W.F. Brilman},
title = {Process optimization of a fixed bed reactor system for direct air capture},
journal = {International Journal of Greenhouse Gas Control},
year = {2021},
volume = {110},
publisher = {Elsevier},
month = {sep},
url = {https://doi.org/10.1016/j.ijggc.2021.103431},
pages = {103431},
doi = {10.1016/j.ijggc.2021.103431}
}