4.8 Article

Microchemical Engineering in a 3D Ordered Channel Enhances Electrocatalysis

Journal

JOURNAL OF THE AMERICAN CHEMICAL SOCIETY
Volume 143, Issue 32, Pages 12600-12608

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/jacs.1c04653

Keywords

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Funding

  1. National Natural Science Foundation of China [21761132008, 21431006, 21922204, 21771168, 21790350, 21973085, 21833007, 22005285]
  2. Foundation for Innovative Research Groups of the National Natural Science Foundation of China [21521001]
  3. Key Research Program of Frontier Sciences, CAS [QYZDJ-SSW-SLH036]
  4. Ministry of Science and Technology of China [2018YFA0208702]
  5. Hefei Science Center of CAS [2015HSC-UE007]
  6. Fundamental Research Funds for the Central Universities [WK2100000005]
  7. the Joint Funds from Hefei National Synchrotron Radiation Laboratory [UN2018LHJJ]
  8. National Postdoctoral Program for Innovative Talents [BX20200316]
  9. China Postdoctoral Science Foundation [2020M671869]

Ask authors/readers for more resources

The kinetics of electrode reactions play a crucial role in electrocatalysis, with challenges remaining in optimizing catalyst kinetics; a comprehensive kinetic model and microchemical engineering strategy can help achieve kinetic optimization; experimental measurements confirm the impact of optimized channel sizes on mass transfer and surface reactions.
The kinetics of electrode reactions including mass transfer and surface reaction is essential in electrocatalysis, as it strongly determines the apparent reaction rates, especially on nanostructured electrocatalysts. However, important challenges still remain in optimizing the kinetics of given catalysts with suitable constituents, morphology, and crystalline design to maximize the electrocatalytic performances. We propose a comprehensive kinetic model coupling mass transfer and surface reaction on the nanocatalyst-modified electrode surface to explore and shed light on the kinetic optimization in electrocatalysis. Moreover, a theory-guided microchemical engineering (MCE) strategy has been demonstrated to rationally redesign the catalysts with optimized kinetics. Experimental measurements for methanol oxidation reaction in a 3D ordered channel with tunable channel sizes confirm the calculation prediction. Under the optimized channel size, mass transfer and surface reaction in the channeled microreactor are both well regulated. This MCE strategy will bring about a significant leap forward in structured catalyst design and kinetic modulation.

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