2021
DOI: 10.1016/j.ijthermalsci.2021.106991
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Natural convection of a viscoplastic fluid in an enclosure filled with solid obstacles

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Cited by 17 publications
(13 citation statements)
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“…The numerical investigation by Kefayati [ 39 ] aims to report the effects that the variation of parameters such as Bingham number ( Bn = 0–4), Rayleigh number ( Ra = 10 4 –10 6 ), Darcy number ( Da = 10 2 –10 6 ), porosity ( φ = 0.1–0.9), Lewis number ( Le = 2.5–100), Buoyancy ratio (N = 0.1–20) and Prandtl number (Pr = 1–100) have on heat and mass transfer. The results corroborate what is reported in closed cavities [ [31] , [32] , [33] , [34] , [35] , [36] , [37] , [38] ]; the heat transfer increases and the unyielded regions decrease with increasing Ra , Le and N.…”
Section: Introductionsupporting
confidence: 90%
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“…The numerical investigation by Kefayati [ 39 ] aims to report the effects that the variation of parameters such as Bingham number ( Bn = 0–4), Rayleigh number ( Ra = 10 4 –10 6 ), Darcy number ( Da = 10 2 –10 6 ), porosity ( φ = 0.1–0.9), Lewis number ( Le = 2.5–100), Buoyancy ratio (N = 0.1–20) and Prandtl number (Pr = 1–100) have on heat and mass transfer. The results corroborate what is reported in closed cavities [ [31] , [32] , [33] , [34] , [35] , [36] , [37] , [38] ]; the heat transfer increases and the unyielded regions decrease with increasing Ra , Le and N.…”
Section: Introductionsupporting
confidence: 90%
“…Focusing on the effects of each geometry, the Prandtl number Pr and the fluid-solid thermal conductivity ratio κ were kept constant. s. It is important to note that the ratio of the thermal conductivity of the fluid used is ten times smaller than the thermal conductivity of the solid body ( ); this ratio represents a realistic order of magnitude for many possible solid materials, such as concrete, sandstone, and stainless steel [ 38 ]. As defined by Eq.…”
Section: Resultsmentioning
confidence: 99%
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“…The findings indicated that the employing nanofluid guides to progress Nusselt number. While Santos et al 33 given the findings of free convective in a duct containing many hot square obstacles, Alturaihi et al 34 given the solutions of free convective in a cold duct containing circular obstacles and hot sheet set at the center of the duct and Javadzadegan et al 35 numerically examined convective heat transfer in a vented duct contains elliptical obstacles to confirm the impact of including porous medium on Nu . Subhash et al 36 focused on the free convection in a porous channel containing a couple of vertical diathermal partitions discrete at equal distance from the duct center.…”
Section: Introductionmentioning
confidence: 99%