2000
DOI: 10.1002/1097-0363(20000815)33:7<939::aid-fld38>3.0.co;2-#
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Finite difference scheme for the solution of fluid flow problems on non‐staggered grids

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Cited by 20 publications
(12 citation statements)
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“…If the term is computed in that form the pressure contributes to the cell mass balance with a strict (dissipative) fourth order derivative, as opposed to the third order derivative of the other form due to the (not always slight) variation of A u P |i . The amount of dissipation is sometimes controlled by a coefficient (other than the geometric factor) that is adjusted ad hoc [19] [20] [24]. In the computational exercices to be presented with the unsteady version of this scheme we prefer to be consistent and stick to the correct expression given in Eq.…”
Section: Cell Face Velocity Expression Steady Casementioning
confidence: 99%
See 1 more Smart Citation
“…If the term is computed in that form the pressure contributes to the cell mass balance with a strict (dissipative) fourth order derivative, as opposed to the third order derivative of the other form due to the (not always slight) variation of A u P |i . The amount of dissipation is sometimes controlled by a coefficient (other than the geometric factor) that is adjusted ad hoc [19] [20] [24]. In the computational exercices to be presented with the unsteady version of this scheme we prefer to be consistent and stick to the correct expression given in Eq.…”
Section: Cell Face Velocity Expression Steady Casementioning
confidence: 99%
“…The actual u * e equation they employed contains some unnecessary approximations that can produce a less accurate solution. Barton et al [19] did not derive a special interpolation procedure for u * e , however they eventually assemble a continuity equation for an unsteady problem that contains factors like ∆V i /A u P |i and not ∆V i / A u P |i 2…”
Section: The Interface Velocity In An Unsteady Flowmentioning
confidence: 99%
“…This is zero for the present problem because all boundaries are solid walls. Therefore the sum of the 16 right hand sides of (6.8) should also be zero, but this is not guaranteed by the present method as described so far. The sum Pτ m h,ΡΔΩP equals zero because the truncation error of the approximation of the mass flux through a face f contributes with opposite sign to the continuity truncation errors of the CVs on either side of f. Also, the sum Pτ2h h,m ,Ρ ΔΩP over all CVs P of the coarse grid 2h is zero because the mass fluxes F2h which are calculated from the restricted velocity and pressure fields contribute with opposite sign to the relative truncation errors of the CVs on either side of the face.…”
Section: Flow Between Concentric Cylindersmentioning
confidence: 92%
“…e.g. [1][2][3][4][5][6][7]). While finite difference, finite element and finite volume methodologies have been extensively developed, the majority of the early fundamental research work in this field was based on finite difference formulations, whereas the finite volume method dominates more recent activity and the commercial codes used in industry.…”
Section: Introductionmentioning
confidence: 99%