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Mathematical Modeling of Laminar and Turbulent Single-phase and Two-phase Flows in Straight and Helical Ducts

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Figure

Figure 2.1 Schematic diagram of the composite parallel-plate channel
Figure 2.4 Dependence of the Nusselt number on the dimensionless position of the interface (a) and the dimensionless half width of the channel (b) for the isoflux wall case
Figure 2.5 Distributions of the dimensionless velocity (a) and the dimensionless effective thermal ξ=
Figure 2.6 Dependence of the Nusselt number on the Darcy number (a), the Forchheimer coefficient (b), and the dimensionless experimental constant in the correlation for thermal dispersion (c) for the isoflux wall case
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