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Journal Articles
Journal Articles
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( a ) Dual-height plate-fin heat sinks glued to a base plate oriented verti...
Published Online: September 22, 2022
Fig. 1 ( a ) Dual-height plate-fin heat sinks glued to a base plate oriented vertically and ( b ) flow channel cross section with conventional kind of fin heat sink ( H 1 * = 1) and dual-height ( H 1 * < 1) fin heat sink More
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Isotherms of fins for  H  1 * = 1.0, ( a )  S *   = 0.1,  H  = 0.04 m; ( b ...
Published Online: September 22, 2022
Fig. 4 Isotherms of fins for H 1 * = 1.0, ( a ) S * = 0.1, H = 0.04 m; ( b ) S * = 0.1, H = 0.05 m; ( c ) S * = 0.3, H = 0.04 m; ( d ) S * = 0.3, H = 0.05 m; ( e ) S * = 0.5, H = 0.04 m; and ( f ) S * = 0.5, H = 0.05 m More
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Comparison of Reynolds evaluation for both NCM and FDM: ( a )  S  *  = 0.1,...
Published Online: September 22, 2022
Fig. 6 Comparison of Reynolds evaluation for both NCM and FDM: ( a ) S * = 0.1, H = 0.04 m, W in,mix = 2197; ( b ) S * = 0.1, H = 0.05 m, W in,mix = 2747; ( c ) S * = 0.3, H = 0.04 m, W in,mix = 2197; ( d ) S * = 0.3, H = 0.05 m, W in,mix = 2747; ( e ) S * = 0.5,... More
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Isocontour of velocity for forced convection velocity components obtained f...
Published Online: September 22, 2022
Fig. 7 Isocontour of velocity for forced convection velocity components obtained from both NCM and FDM: ( a ) S * = 0.1 , H 1 * = 1.0 , t c * = 0.10 , Z = 0.2891 , H = 0.05 m ; ( b ) S * = 0.1 , H 1 * = 1.0 , t c *... More
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Isotherms of the fluids for forced convection velocity component obtained f...
Published Online: September 22, 2022
Fig. 8 Isotherms of the fluids for forced convection velocity component obtained from both NCM and FDM: ( a ) S * = 0.1 , H 1 * = 1.0 , t c * = 0.10 , Z = 0.2891 , H = 0.05 m ; ( b ) S * = 0.1 , H 1 * = 1.0 , t c... More
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Schematic diagram of the inclined channel (ϴ = 0 deg represents horizontal ...
Published Online: September 22, 2022
Fig. 1 Schematic diagram of the inclined channel (ϴ = 0 deg represents horizontal channel and ϴ = 90 deg indicates a vertically downward channel) More
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( a ) Variation of local Nusselt number along the channel length at Δ T  = ...
Published Online: September 22, 2022
Fig. 3 ( a ) Variation of local Nusselt number along the channel length at Δ T = 5 K and 30 K and ( b ) validation of the present numerical model with the published data of Wang and Rose [ 35 ] More
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Two-phase (liquid−vapor) flow patterns for flow through channel with differ...
Published Online: September 22, 2022
Fig. 8 Two-phase (liquid−vapor) flow patterns for flow through channel with different mass flux conditions for H = 1 mm and g = 9.81 m/s 2 More
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