Abstract:The effect of viscous dissipation and rarefaction on heat transfer characteristics of hydrodynamically and thermally fully developed flow between parallel plates with constant heat flux conditions is analyzed. Three different types of heat flux boundary conditions, i.e., both plates kept at different constant heat fluxes, both plates kept at equal constant heat fluxes, and one plate insulated, are applied. In all cases, closed form expressions are obtained for the temperature distribution and Nusselt number. V… Show more
“…On the contrary, for the case of Br = 0, Kn = 0, the present solution predicts Nu = 2.69, which is exactly same as reported by various researchers [9,17,[36][37][38]. ð Þ $10 À5 À 10 À4 m, O q ð Þ $ 1 À 10 3 W/m 2 : Considering these values, one can evaluate the order of magnitude for Brinkman number as: O Br j j ð Þ$10 1 À 10 À3 [23].…”
Section: Theoretical Analysissupporting
confidence: 91%
“…In addition, for the case of Br = 0, Kn = 0, present solution (Nu = 4.12) reduces the Nusselt number, which is exactly same as reported by various researchers [9,16,[36][37][38].…”
Section: Theoretical Analysissupporting
confidence: 87%
“…Present prediction is validated for the cases that neglect both viscous heating and microscale effects (Kn = 0). For these cases, the Nusselt number is found to be exactly same as reported by earlier researchers [9,16,[36][37][38]. The results obtained from the present analysis are elaborated below.…”
Section: Theoretical Analysissupporting
confidence: 75%
“…While, the fully developed Nusselt number does not vary significantly with the change in the thermophysical properties in the analysis [34,35]. Efforts have been made to study the effect of second order boundary conditions and asymmetric heat flux boundary conditions on the heat transfer characteristics of various geometries such as: parallel plate microchannels and micropipe [36][37][38]. It is observed that the asymmetric heat flux condition significantly alters the temperature profile and singularities in Nusselt number are obtained for various values of Knudsen number [18][19][20].…”
Section: Introductionmentioning
confidence: 86%
“…It is reported that velocity slip and temperature jump affect the heat transfer performance in opposite ways [15]. Also, the studies report the deviation in heat transfer performance by considering the first and second order slip models [36][37][38]. The effect of asymmetric heat flux ratio on the heat transfer ratio and the heat transfer performance has also been reported [9,[18][19][20].…”
This paper reports the hydrodynamically and thermally fully developed, laminar, incompressible, forced convective heat transfer characteristics of gaseous flows through a parallel plate microchannel with different constant heat flux boundary conditions. The first order velocity slip and viscous dissipation effects are considered in the analysis. Here, three different thermal boundary conditions such as: both plates kept at different constant heat fluxes, both plates kept at equal constant heat fluxes and one plate kept at constant heat flux and other one insulated are considered for the analysis. The deviation in Nusselt number between the model that considers both first order velocity slip and temperature jump and the one that considers only velocity slip is reported. Also, the effect of various heat flux ratios on the Nusselt number is reported in this analysis. In addition, the deviation in Nusselt number between first and second order slip model is discussed in this study.
“…On the contrary, for the case of Br = 0, Kn = 0, the present solution predicts Nu = 2.69, which is exactly same as reported by various researchers [9,17,[36][37][38]. ð Þ $10 À5 À 10 À4 m, O q ð Þ $ 1 À 10 3 W/m 2 : Considering these values, one can evaluate the order of magnitude for Brinkman number as: O Br j j ð Þ$10 1 À 10 À3 [23].…”
Section: Theoretical Analysissupporting
confidence: 91%
“…In addition, for the case of Br = 0, Kn = 0, present solution (Nu = 4.12) reduces the Nusselt number, which is exactly same as reported by various researchers [9,16,[36][37][38].…”
Section: Theoretical Analysissupporting
confidence: 87%
“…Present prediction is validated for the cases that neglect both viscous heating and microscale effects (Kn = 0). For these cases, the Nusselt number is found to be exactly same as reported by earlier researchers [9,16,[36][37][38]. The results obtained from the present analysis are elaborated below.…”
Section: Theoretical Analysissupporting
confidence: 75%
“…While, the fully developed Nusselt number does not vary significantly with the change in the thermophysical properties in the analysis [34,35]. Efforts have been made to study the effect of second order boundary conditions and asymmetric heat flux boundary conditions on the heat transfer characteristics of various geometries such as: parallel plate microchannels and micropipe [36][37][38]. It is observed that the asymmetric heat flux condition significantly alters the temperature profile and singularities in Nusselt number are obtained for various values of Knudsen number [18][19][20].…”
Section: Introductionmentioning
confidence: 86%
“…It is reported that velocity slip and temperature jump affect the heat transfer performance in opposite ways [15]. Also, the studies report the deviation in heat transfer performance by considering the first and second order slip models [36][37][38]. The effect of asymmetric heat flux ratio on the heat transfer ratio and the heat transfer performance has also been reported [9,[18][19][20].…”
This paper reports the hydrodynamically and thermally fully developed, laminar, incompressible, forced convective heat transfer characteristics of gaseous flows through a parallel plate microchannel with different constant heat flux boundary conditions. The first order velocity slip and viscous dissipation effects are considered in the analysis. Here, three different thermal boundary conditions such as: both plates kept at different constant heat fluxes, both plates kept at equal constant heat fluxes and one plate kept at constant heat flux and other one insulated are considered for the analysis. The deviation in Nusselt number between the model that considers both first order velocity slip and temperature jump and the one that considers only velocity slip is reported. Also, the effect of various heat flux ratios on the Nusselt number is reported in this analysis. In addition, the deviation in Nusselt number between first and second order slip model is discussed in this study.
Effects of slip velocity and volume fraction of slip spheres on the momentum transfer characteristics of assemblages of slip spheres are numerically investigated. The fluid slip along the surface of the sphere is considered by Navier's linear slip model. The dimensionless governing continuity and momentum equations are solved using a semi-implicit marker and cell method implemented on a staggered grid arrangement in spherical coordinates. The convection and viscous terms of momentum equations are discretized by means of the QUICK scheme and a second-order central differencing scheme, respectively. The present numerical solver is benchmarked via grid independence and comparisons with the existing literature values. Results were obtained over a wide range of pertinent dimensionless numbers such as the Reynolds number, volume fraction of the dispersed phase, and dimensionless slip parameter.
The effect of shear work at solid boundaries for parallel plates and a micropipe is considered to analyze the heat transfer characteristics in the slip flow region for gaseous flow. The fluid flow is assumed to be laminar, incompressible, steady, and hydrodynamically and thermally fully developed. The effects of second-order velocity slip, temperature jump, shear work at the solid surface, and viscous dissipation are considered. The constant heat flux boundary condition is used at the surface of the parallel plates and of the micropipe. Closed-form expressions are obtained for the temperature distribution and Nusselt number as a function of various modeling parameters for both geometries. The results show that neglecting the shear work underpredicts the Nusselt number.
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