Transport Phenomena · Local conservation laws, constitutive fluxes, and scaling
An incompressible liquid approaches a porous flat surface with an accelerating external…
Problem
An incompressible liquid approaches a porous flat surface with an accelerating external velocity (U_e(x)=Kx^{1/3}), where (K=3.20\ \mathrm{m^{2/3}\,s^{-1}}) and (x) is measured from the leading edge. Uniform suction into the surface has magnitude (V_s=2.00\times10^{-3}\ \mathrm{m\,s^{-1}}), so the wall-normal velocity at the wall is (v_w=-V_s). The liquid has kinematic viscosity (8.50\times10^{-7}\ \mathrm{m^2\,s^{-1}}) and density (990\ \mathrm{kg\,m^{-3}}). Model the laminar boundary layer with (u/U_e=2\eta-2\eta^3+\eta^4), where η=y/δ for (0\le\eta\le1). Starting from the momentum-integral equation with wall mass transfer, derive the differential equation governing (\delta(x)) and integrate it numerically from (x_0=1.00\ \mathrm{mm}) to (x=0.500\ \mathrm{m}). Use the initial condition that at (x_0), (\delta) equals the no-suction similarity value obtained by retaining the given velocity profile and setting (V_s=0). Report (\delta), displacement thickness, momentum thickness, wall shear stress, and local skin-friction coefficient at (x=0.500\ \mathrm{m}). Also determine the percentage change in wall shear stress relative to the corresponding no-suction result at that location.
Hint
In the momentum-integral equation, suction enters through \(v_w/U_e=-V_s/U_e\).
Check your work
Work the problem yourself first. Then open it in Training to check your answer and read the full worked solution.
Create a free account to check your answer and see the solution. Create a free account.
More Transport Phenomena practice problems
- A Newtonian oil of density 860 kg/m^3 and viscosity 0.145 Pa s flows steadily through a…Local conservation laws, constitutive fluxes, and scaling
- A counterflow double-pipe heat exchanger cools 0.900 kg/s of a liquid process stream…Local conservation laws, constitutive fluxes, and scaling
- A spherical crystal of initial radius 6.00 mm and density 1200 kg/m^3 dissolves in a…Momentum transport and viscous flow
- A water film flows down a 0.500 m wide heated strip of length 2.00 mMomentum transport and viscous flow
- Hot water flows turbulently over one face of a flat plateMomentum transport and viscous flow
- A homogeneous half-space y>0 has thermal diffusivity α=1× 10^(-6) m^2/s and…Energy transport and convection-conduction coupling
- Two well-mixed compartments exchange a dilute solute through a membraneSpecies transport, diffusion, and convection
- A solute is carried down a straight circular tube of radius a=0.001 m by a fully…Species transport, diffusion, and convection
- A liquid element is exposed to a solute for a single contact time t_c=4 sBoundary layers and interfacial transfer coefficients