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The effect of Stefan flow on Nusselt number and drag coefficient of spherical particles in non-isothermal gas flow

Sammendrag

A Stefan flow can be generated during a phase change or reactions of a particle immersed in a fluid. This study investigates the effect of Stefan flow on the exchange of momentum (drag coefficient (CD)) and heat transfer (Nusselt number (Nu)) between the particle and bulk-fluid. Fully resolved simulations were carried out for a flow near a spherical particle immersed in a uniform bulk flow. The immersed boundary method is used for implementing fluid-solid interactions and the particle is considered as a static boundary with fixed boundary conditions. In a non-isothermal flow, the changes in thermophysical properties at the boundary layer played a role in the variation of CD and Nu by a Stefan flow further. The previously developed model for the drag coefficient of a spherical particle in a uniform isothermal flow was modified for a uniform non-isothermal flow. The model is developed based on physical interpretation. A new model is developed for the Nusselt number for a spherical particle with a uniform Stefan flow combining available models in literature. The models are validated for Stefan Reynolds number −8⩽Resf,p⩽25 and particle Reynolds number of 2⩽Ref⩽30 in gas flow (i.e. Pr≈0.7). © 2021 The Author(s)
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Kategori

Vitenskapelig artikkel

Oppdragsgiver

  • Research Council of Norway (RCN) / 267916
  • Sigma2 / NN9405K
  • EC/H2020 / 764697

Språk

Engelsk

Forfatter(e)

  • Thamali R. Jayawickrama
  • Nils Erland L. Haugen
  • Matthâus Ulrich Bäbler
  • Muhammad Aqib Chishty
  • Kentaro Umeki

Institusjon(er)

  • Luleå tekniska universitet
  • Norges teknisk-naturvitenskapelige universitet
  • SINTEF Energi AS / Termisk energi
  • Kungliga Tekniska högskolan

År

2021

Publisert i

International Journal of Multiphase Flow

ISSN

0301-9322

Årgang

140

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