Numerical solutions are presented for a laminar steady three-dimensional boundary-layer flow of non-Newtonian fluid over a convective stretching surface in the presence of nanoparticles. The effects of an internal heat generation/ absorption, thermal radiation, Brownian motion, and thermophoresis are also taken into account. The viscoelastic fluid model is employed to describe the non-Newtonian fluid. The governing partial differential equations are reduced to a set of four coupled nonlinear ordinary differential equations using suitable similarity transformations. The resultant equations are solved numerically by employing the well-known Runge-Kutta-Fehlberg method with the shooting technique. The effect of pertinent parameters on skin friction coefficient in the x and y directions, local Nusswelt number, local Sherwood number, velocity in the x and y directions, temperature, and nanoparticle volume fraction profile are studied and discussed in detail.
Nomenclature
C= nanoparticle volume fraction, kg∕m 3 C fx , C fy = skin friction coefficient along x and y directions C w = concentration of nanoparticles at the walldimensionless velocity component g = acceleration due to gravity, m∕s 2 h f = heat transfer coefficient j w = nanoparticles mass flux k = thermal conductivity, W∕m · K k 0 = material fluid parameter k 1 = mean absorption coefficient, m −1 Le = Lewis number Nb = Brownian motion parameter Nt = thermophoresis parameter Nu x = local Nusselt number Pr = Prandtl number Q = heat source/sink parameter Q 0 = heat source/sink coefficient q r = radiative heat flux, W · m −2 q w = heat flux R = thermal radiation parameter Re x = local Reynolds number Sh = Sherwood number T = fluid temperature, K T f = surface temperature, K T ∞ = ambient fluid temperature, K u, v, w = velocity components along, y, and z directions, m · s −1 x, y, z = coordinate along the plate, m α m= thermal diffusivity of the fluid η = similarity variable θ = dimensionless temperature μ = dynamic viscosity, kg · m −1 · s −1 ν = kinematic viscosity, m 2 · s −1 ρ f = density of the base fluid, kg∕m 3 ρ p = density of the particles, kg∕m 3 σ = Stefan-Boltzmann constant, W · m −2 · K −4 τ = ratio of the heat capacity of the nanoparticle and that of ordinary fluid τ wx , τ wy = surface shear stress along x and y directions ϕ = dimensionless nanoparticle volume fraction ψ = stream function Superscript 0 = derivative with respect to η