Two-Step Conversion of CO2 to Light Olefins: Laboratory-Scale Demonstration and Scale-Up Considerations
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A1 Alkuperäisartikkeli tieteellisessä aikakauslehdessä
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Date
2022-12
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Language
en
Pages
15
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ChemEngineering, Volume 6, issue 6
Abstract
The highly selective production of light olefins from CO2 was demonstrated for the first time with a laboratory-scale process comprising consecutive reverse water gas shift (RWGS) and Fischer–Tropsch (FT) reactors. The RWGS reaction, catalyzed by rhodium washcoated catalyst at 850 °C yielded good quality syngas with conversion values close to the thermodynamic equilibrium and without experiencing catalyst deactivation from carbon formation or sintering. For the FT synthesis, a packed bed Fe-Na-S/α-Al2O3 catalyst was used. The highest light olefin selectivity observed for the FT-synthesis was 52% at 310 °C, GHSV of 2250 h−1 and H2/CO ratio of 1. However, the optimal conditions for the light olefin production were determined to be at 340 °C, a GHSV of 3400 h−1 and a H2/CO ratio of 2, as the CO conversion was markedly higher, while the light olefin selectivity remained at a suitably high level. In addition to the experimental results, considerations for the further optimization and development of the system are presented. The combined RWGS–FT process seems to work reasonably well, and initial data for basic process design and modeling were produced.Description
Funding Information: This work was supported by the BECCU project (https://www.beccu.fi/) (accessed on 1 October 2022), which received funding from Business Finland (Funding decision number 3834/31/2019). Publisher Copyright: © 2022 by the authors.
Keywords
Fischer–Tropsch synthesis, FTO, light olefins, reverse water gas shift, RWGS
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Citation
Reinikainen, M, Braunschweiler, A, Korpilo, S, Simell, P & Alopaeus, V 2022, ' Two-Step Conversion of CO 2 to Light Olefins: Laboratory-Scale Demonstration and Scale-Up Considerations ', ChemEngineering, vol. 6, no. 6, 96 . https://doi.org/10.3390/chemengineering6060096