Nu/Sh correlation for
particle-liquid heat and mass transfer
coefficients
in trickle beds based on Péclet similarity
F. Larachi,* C. Alix, , B.P.A. Grandjean, A. Bernis
Department of Chemical Engineering and
CERPIC; Laval University, Ste-Foy, Canada PQ G1K 7P4
&Laboratoire de génie des procédés, Université de Savoie, Domaine
Scientifique, 73376 Le Bourget du Lac, France
Chem. Eng. Res. Des. (Trans IChemE part A), 81 , 689-694 (2003)
*Corresponding
author (Email: flarachi@gch.ulaval.ca)
Tel.
1-418-656-3566; Fax 1-418-656-5993
Abstract Knowledge of the particle to liquid
heat and mass transfer coefficients in trickle beds is important particularly
in contexts where exothermic reactions impede liquid replenishment over dried
spots in the catalyst bed, or when the transport, especially in liquid-limited
reactions, is curbed by excessive liquid-solid interfacial resistance. Although
particle-liquid heat and mass transfer coefficients in trickle beds are linked
to each other, the known Chilton-Colburn analogy or alike failed to yield a
single Nu/Sh correlation to quantify both heat and
mass transfer phenomena at the pellet scale. In this work, a single correlation
embedding the heat and mass transfer information into a Péclet
number was derived and validated over 1259 particle-liquid heat and mass
transfer coefficients in trickle beds. Depending on whether a heat or a mass Péclet number is used, the proposed correlation predicted
Nu and Sh numbers with average absolute relative
errors of 18% and 22%, respectively. In particular, when equal heat and mass Péclet numbers occur, under physically and geometrically
similar conditions, the correlation predicts true analogy between heat and mass
transfer at the pellet level.
Download
the simulator for computing: tbr-nush.zip
You may also download our Excel worksheets simulators for Trickle-bed or Flooded
Bed reactors.
The neural
correlation was developped with the software NNFit