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Computing non-Newtonian fluid flow with radial basis function networks

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Figure

Table 1: Rectilinear flow of power-law fluid in a square duct: comparison of the frictionfactorAll predictions are in good agreement over a wide range of fRe between the IRBFN method using 27 × 27 data points and other methods
Table 2: Non-rectilinear flow of CEF fluid in a square duct: the extreme values of thevelocity components and the stream function.
Table 3: “Wiggly” tube problem, Newtonian fluid, Reflow resistance by the present method and other methods for several geometries
Table 4: “Wiggly” tube problem (ϵ = 0.3; N = 0.16), Newtonian fluid: the computedflow resistance by the IRBFN method for a wide range of Re.
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