Microwave-assisted, performance-advantaged electrification of propane dehydrogenation


Journal article


Yeonsu Kwak, Cong Wang, Chaitanya A Kavale, Kewei Yu, Esun Selvam, R. Mallada, J. Santamaría, I. Julian, J. Catalá-Civera, Himanshu Goyal, Weiqing Zheng, D. Vlachos
Science Advances, 2023

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APA   Click to copy
Kwak, Y., Wang, C., Kavale, C. A., Yu, K., Selvam, E., Mallada, R., … Vlachos, D. (2023). Microwave-assisted, performance-advantaged electrification of propane dehydrogenation. Science Advances.


Chicago/Turabian   Click to copy
Kwak, Yeonsu, Cong Wang, Chaitanya A Kavale, Kewei Yu, Esun Selvam, R. Mallada, J. Santamaría, et al. “Microwave-Assisted, Performance-Advantaged Electrification of Propane Dehydrogenation.” Science Advances (2023).


MLA   Click to copy
Kwak, Yeonsu, et al. “Microwave-Assisted, Performance-Advantaged Electrification of Propane Dehydrogenation.” Science Advances, 2023.


BibTeX   Click to copy

@article{yeonsu2023a,
  title = {Microwave-assisted, performance-advantaged electrification of propane dehydrogenation},
  year = {2023},
  journal = {Science Advances},
  author = {Kwak, Yeonsu and Wang, Cong and Kavale, Chaitanya A and Yu, Kewei and Selvam, Esun and Mallada, R. and Santamaría, J. and Julian, I. and Catalá-Civera, J. and Goyal, Himanshu and Zheng, Weiqing and Vlachos, D.}
}

Abstract

Nonoxidative propane dehydrogenation (PDH) produces on-site propylene for value-added chemicals. While commercial, its modest selectivity and catalyst deactivation hamper the process efficiency and limit operation to lower temperatures. We demonstrate PDH in a microwave (MW)–heated reactor over PtSn/SiO2 catalyst pellets loaded in a SiC monolith acting as MW susceptor and a heat distributor while ensuring comparable conditions with conventional reactors. Time-on-stream experiments show active and stable operation at 500°C without hydrogen addition. Upon increasing temperature or feed partial pressure at high space velocity, catalysts under MWs show resistance in coking and sintering, high activity, and selectivity, starkly contrasting conventional reactors whose catalyst undergoes deactivation. Mechanistic differences in coke formation are exposed. Gas-solid temperature gradients are computationally investigated, and nanoscale temperature inhomogeneities are proposed to rationalize the different performances of the heating modes. The approach highlights the great potential of electrification of endothermic catalytic reactions.


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