2005
DOI: 10.1016/j.jaerosci.2004.12.002
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On the mixed convection hydrodynamic force on a sphere

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Cited by 12 publications
(6 citation statements)
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“…Our results for drag coefficient for Re P 1, presented in Fig. 16b, does not follow the empirical formula due to Mograbi and Bar-Ziv [26,27]. Thus, for the range of Gr considered in this paper a weak non-linearity assumption for the mixed convection flow is not valid.…”
Section: Resultscontrasting
confidence: 60%
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“…Our results for drag coefficient for Re P 1, presented in Fig. 16b, does not follow the empirical formula due to Mograbi and Bar-Ziv [26,27]. Thus, for the range of Gr considered in this paper a weak non-linearity assumption for the mixed convection flow is not valid.…”
Section: Resultscontrasting
confidence: 60%
“…The drag coefficient at low Reynolds number, which is mainly due to the viscous force, is enhanced with the increase of Ri. Based on the weak interaction between free and forced convection Mograbi and BarZiv [26,27] proposed an empirical expression for the hydrodynamic drag on a sphere at low range of Reynolds number and Grashof number. They compared the empirical formula with the numerical result for Gr = 10 À2 and 10 À4 with 0 6 Ri 6 1 and found a large discrepancy when Ri is O(1) at Gr = 10 À2 .…”
Section: Resultsmentioning
confidence: 99%
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“…Wong et al [106] solved the full Navier-Stokes and energy equation of an isothermal sphere in combined convection by a finite element method. We mention also the relatively recent papers on this problem by Jenny and Dušek [115], Jenny et al [116], Mograbi and Bar-Ziv [117], [118] and Mebarek et al [119]. Later, Kumari and Nath [108] studied the unsteady mixed convection with double diffusion over a horizontal cylinder and sphere within a porous medium.…”
Section: Introductionmentioning
confidence: 98%
“…An analytical solution is rarely obtained in such a configuration. Mograbi and Bar-Ziv [5] have shown that a approximated solution can be obtained by the way of dimensionless numbers: the Grashof number is useful to estimate the natural convection effects. As mixed convection occurs in the present problem, heat transfer must be defined by both Re and Gr numbers.…”
Section: Introductionmentioning
confidence: 99%