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Wake dynamics and forced convective heat transfer characteristics past a semi-circular cylinder at incidence have been investigated numerically. Utilizing air as an operating fluid computations are carried out for wide ranges of the Reynolds number (80 ? Re ? 180) and angle of incidences (0 ? α ? 180°). Angle of incidence reveals three flow separation zones. Structure properties of shear layer and vortex motions on each flow separation zones are analyzed critically. Functional dependence of drag (CD), lift (CL), and moment (CM) coefficients on the angle of incidence is explored and analyzed in detail. Increase in angle of incidence increases streamline curvature. A structural similarity is observed between the contours of vorticity and the corresponding isotherms. Strouhal number shows a decreasing trend up to certain values of α and thereafter it increases marginally. A new correlation of Strouhal number as a function of Re and α has been established for the present range of Reynolds numbers. At the singularity points a sudden jump in local Nusselt number distribution is observed. The trend of variation of average Nusselt number with α is similar to that of Strouhal number variation. The average Nusselt number is found to vary as Re0.529(1+α)-0.0476.  相似文献   

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Heat transfer measurements from a rotating two-pass square channel with two opposite leading and trailing walls roughened by 45° parallel ribs arranged in the staggered manner are performed to examine the effects of Reynolds (Re), rotation (Ro) and buoyancy (Bu) numbers on local and area-averaged Nusselt numbers (Nu and Nu¯). Full-field Nu distributions over the two rib-roughened leading and trailing walls are measured at the conditions of 4000 ? Re ? 16,000, 0 ? Ro ? 0.8 and 0.0015 ? Bu ? 0.93 (0.05 ? Δρ/ρ ? 0.1) using the infrared thermography which allows for the detailed examination of the Coriolis and rotating buoyancy effects on Nu distributions over the rotating ribbed surface. Selected heat transfer data in term of Nu ratio between rotating and stationary levels illustrates the influences of rotation on local and area-averaged heat transfer performances. Area-averaged Nu¯ for the turn region and the inlet and outlet ribbed legs of the rotating two-pass channel are parametrically analyzed to devise a set of empirical heat transfer correlations that permits the evaluation of the interdependent and individual effects of Re, Ro and Bu on Nu¯.  相似文献   

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This paper measures high-pressure turbulent burning velocities (ST) of lean methane spherical flames at constant turbulent Reynolds numbers (ReT  uLI/ν), where u′ and LI are the r.m.s. turbulent fluctuation velocity and the integral length scale of turbulence and ν is the kinematic viscosity of reactants. This is achieved by adopting a recently-built double-chamber, fan-stirred cruciform burner with perforated plates that can be used to generate intense near-isotropic turbulence with negligible mean velocities while controlling the product of uLI in proportion to the decreasing ν at elevated pressure (p) up to 1.2 MPa. Results show that when ReT is fixed ranging from 6700 to 14,200, values of ST decrease similarly as laminar burning velocities (SL) with increasing p in minus exponential manners, revealing a global response of burning velocities to pressure. In general, the higher ReT, the higher ST/SL at any fixed p. It is found that the curves of ST/SL as a function of u′/SL all exhibit very strong bending under constant ReT conditions. These results not only reveal that the important effect of ReT on high-pressure ST/SL enhancement, but also suggest that recent findings related with the promotion effect of increasing pressure on ST primarily due to the enhancement of flame instabilities via the thinner flame without any discussion on the influence of ReT elevation at elevated pressure should be reconsidered. Moreover, we found that the modified values of ST at mean progress variable c¯  0.5 show good agreements between Bunsen-type and spherical flames, suggesting that ST determined at flame surfaces with c¯ = 0.5 may be a better representative of itself regardless of the flame geometries. Finally, various general correlations of ST,c¯=0.5 are compared and discussed. It is found that the present scattering data under different p and ReT conditions can be merged onto a single curve of (ST,c¯=0.5 ? SL)/u = 0.14Da0.47, where Da is the turbulent Damköhler number.  相似文献   

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This paper investigates the combined effect of Prandtl number and Richardson number on the wake dynamics and heat transfer past a circular cylinder in crossflow using a SUPG based finite element method. The computations are carried out for 80 < Re < 180, 0.7 < Pr < 100 and 0?Ri?2. The results have been presented for both forced and mixed convection flows. In the case of forced convection, crowding of temperature contours with reduced spatial spread is observed for increasing Prandtl numbers. The local and average Nusselt numbers are found to increase with increasing Reynolds number and Prandtl number. The average Nusselt number and Colburn factor are found to vary as Re0.548 Pr 0.373 and Re?0.452, respectively. The extrapolated results of the average Nusselt number for low and high Reynolds numbers are found to match quite well with the available results in literature. Effect of Prandtl number shows various interesting phenomena for the mixed convective flows. Increasing the Prandtl numbers resulted in decreasing deflection and strength in the wake structures. The effect of baroclinic vorticity production during vortex shedding has been demonstrated at the vicinity of the cylinder and near wake. The Strouhal number is found to decrease with increasing Prandtl number, in the case of buoyancy induced flow. The effect of increasing Prandtl number is manifested as the stabilizing effect in the flow. This is, perhaps, the first time that such behavior for the Prandtl number is being reported. Additionally it is observed that the average Nusselt number decreases with increasing Richardson number.  相似文献   

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