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- W2011002960 abstract "The influence of the Schmidt number on the wall-to-liquid mass transfer in a packed bed reactor has been studied. It is shown that use of the classical dimensionless group Sh·Sc-13 and the particle Reynolds number ReL as a means of taking the effects of Schmidt number into account was not appropriate. The dimensionless group Sh' · φ · Sc−0.41 · √β and ReLW, based on an appropriate characteristic length and wall porosity were found to represent the wall mass transfer correctly as well as the wall heat-transfer coefficients obtained with different organic liquids." @default.
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- W2011002960 title "Wall-to-liquid mass transfer in a packed-bed reactor: influence of Schmidt number" @default.
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- W2011002960 doi "https://doi.org/10.1016/0255-2701(94)90008-6" @default.
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