2015
DOI: 10.1016/j.proeng.2015.11.444
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MHD Heat and Mass Transfer Flow Over a Stretching Wedge with Convective Boundary Condition and Thermophoresis

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Cited by 20 publications
(14 citation statements)
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“…Here, is measured from the tip of the wedge, is the Falkner-Skan power-law parameter, and = 2 /(1 + ) is the Hartree pressure gradient parameter corresponding to = Ω/ for the total angle Ω of the wedge (see Figure 1). Physically, < 0 corresponding to an adverse pressure gradient (often resulting in boundary layer separation) while > 0 represents favorable pressure gradient (Nagendramma et al [1]). In the Blasius solution = 0 corresponding to an angle of attack of zero radians, where = 1 corresponding to stagnation point flow.…”
Section: Mathematical Formulationmentioning
confidence: 99%
See 1 more Smart Citation
“…Here, is measured from the tip of the wedge, is the Falkner-Skan power-law parameter, and = 2 /(1 + ) is the Hartree pressure gradient parameter corresponding to = Ω/ for the total angle Ω of the wedge (see Figure 1). Physically, < 0 corresponding to an adverse pressure gradient (often resulting in boundary layer separation) while > 0 represents favorable pressure gradient (Nagendramma et al [1]). In the Blasius solution = 0 corresponding to an angle of attack of zero radians, where = 1 corresponding to stagnation point flow.…”
Section: Mathematical Formulationmentioning
confidence: 99%
“…Fluid flows with convective heat and mass transfer over a wedge shaped bodies is ensured in many thermal engineering applications like crude oil extraction, geothermal systems, thermal insulation, heat exchangers, and the storage of nuclear waste, Nagendramma et al [1]. A model of steady laminar fluid flow over a wedge has developed for the first time by Falkner and Skan [2] to illustrate the application of Prandtl's boundary layer theory.…”
Section: Introductionmentioning
confidence: 99%
“…Fluid flows with heat and mass transfer over a wedge shaped bodies is happened in many thermal engineering applications such as heat exchangers, crude oil extraction, thermal insulation, geothermal systems and the storage of nuclear waste [6][7]. In recent times, boundary layer flow of heat and mass transfer of nanofluids over a wedge has become a current topic of interest.…”
Section: Introductionmentioning
confidence: 99%
“…In recent years, a lot of interest has been focused on studying the problem of incompressible steady viscous flow over a non-isothermal wedge because of its wide practical applications in technological processes such as design for power generators, design for cooling of nuclear reactors, construction of heat exchangers, and blood flow measurement techniques [1]. Chamkha et al [2] investigated the steady magneto-hydrodynamic (MHD) forced convective boundary layer flow of a Newtonian, electrically conducting and heat generating/absorbing fluid over a non-isothermal wedge in the presence of thermal radiation effects.…”
Section: Introductionmentioning
confidence: 99%
“…C ∞ -concentration far away from the wedge (-) ∆C -concentration difference (= C w − C ∞ ) (-) C f , x -local skin friction coefficient = f (0) (n + 1)/2Re x (-) C P -specific heat at constant pressure (J kg −1 K −1 ) D -concentration diffusion coefficient (m 2 s −1 ) Ec -Eckert number = u 2 w (x)/C P (T w − T ∞ ) (-) f -dimensionless stream-function = ψ(x, y) (n + 1)/(2νxu w ) (-) f -dimensionless velocity variable (= u/u w (x)) (-) k -thermal conductivity (W m −1 K −1 ) l 1 -temperature jump coefficient (m −1 ) n -exponent of stretching velocity of the wedge (-) Nu x -local Nusselt number = −θ (0) (n + 1)Re x /2 (-) N s -entropy generation number (-) (N s ) th -entropy generation due to heat transfer (-) N fr -entropy generation due to fluid friction (-) -suction/injection velocity along y-axis x -x-axis aligned along the stretching wedge (m) y -y-axis aligned normal to the stretching wedge (m) Greek symbols α -thermal diffusivity (m 2 s −1 ) β -wedge angle parameter (= 2n/(n + 1)) (-) γ -chemical reaction rate parameter (= 2κx/[(n + 1)u w ] ) (-) ε -dimensionless constant parameter (= (RDC ∞ )/k) (-) η -similarity variable = y (n + 1)u w /(2νx) (-) θ -dimensionless temperature variable (= (T − T ∞ )/(T w − T ∞ ) ) (-) λ -velocity ratio parameter (= a/c) (-)…”
mentioning
confidence: 99%