Decoupling the relative rate of hydrogen uptake via convection and mass transfer by a single catalytic pellet in a scaled down trickle bed reactor

White, JP orcid.org/0000-0002-8093-8298, Chamberlain, TW orcid.org/0000-0001-8100-6452, Bourne, RA orcid.org/0000-0001-7107-6297 et al. (3 more authors) (2020) Decoupling the relative rate of hydrogen uptake via convection and mass transfer by a single catalytic pellet in a scaled down trickle bed reactor. Chemical Engineering Journal, 394. 124920. ISSN 1385-8947

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Copyright, Publisher and Additional Information: © 2020 Elsevier B.V. This is an author produced version of a paper published in Chemical Engineering Journal. Uploaded in accordance with the publisher's self-archiving policy.
Keywords: Heterogeneous hydrogenation; Mass transfer; Trickle bed reactors; Scaling down; Single pellet
Dates:
  • Published: 15 August 2020
  • Accepted: 30 January 2020
  • Published (online): 4 February 2020
Institution: The University of Leeds
Academic Units: The University of Leeds > Faculty of Engineering & Physical Sciences (Leeds) > School of Chemical & Process Engineering (Leeds)
The University of Leeds > Faculty of Engineering & Physical Sciences (Leeds) > School of Chemistry (Leeds) > Inorganic Chemistry (Leeds)
Depositing User: Symplectic Publications
Date Deposited: 03 Feb 2020 15:57
Last Modified: 04 Feb 2021 01:39
Status: Published
Publisher: Elsevier
Identification Number: https://doi.org/10.1016/j.cej.2020.124290

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