- #1
fahraynk
- 186
- 6
Homework Statement
An alternative to the usual no-slip wall boundary condition ##u = 0, v = 0##, is the porous-wall condition ##u = 0##, ##v = v_w(x)##. A porous wall with negative ##v_w## (suction) is known to delay transition to turbulence, for example.
1a) Assuming a uniform ##u_e(x)##, determine what differential equation needs to be satisfied by a self-similar boundary layer solution for a nonzero vw. Assume that ##v_w≪u_e## so that the TSL equations remain valid.
1b) Determine the restrictions that must be placed on ##v_w(x)## so that the similar boundary layer solution you derived in Part a) can occur.
1c) Now assuming a non-uniform ##u_e(x)## determine what differential equation needs to be satisfied by a self-similar boundary layer solution for a nonzero ##v_w##
1d) Determine the restrictions that must be placed on ##v_w(x)## and ##u_e(x)## so that the similar boundary
layer solution you derived in Part c) can occur.
Homework Equations
density, pressure, velocity in x, velocity in y, velocity external, viscosity = ##\rho##,##P##,##u##,##v##,##u_e##,##\vartheta##
##X_y=\frac{\partial X}{\partial Y}##
stream function : ##-\phi_x=v##, ##\phi_y=u##
stream function form of thin shear equations :
$$\phi_y * \phi_{xy} - \phi_x*\phi_{yy}=U_e*\frac{\partial U_e}{\partial x}+\vartheta * \phi_{yyy}$$
The Attempt at a Solution
So the answer for "non self similar solution" would be the regular thin shear layer equations with a boundary condition at the wall of ##v(y=0)=v_w##
$$u_x+u_y=0\\\\
u_t+u*u_x+v*u_y=-\frac{1}{\rho}P_x+\vartheta*u{yy}$$
with a solution ##u=u_e[1-e^\frac{v_wy}{\vartheta}]##
But the question wants to know the equation that needs to be solved by a self similar solution.
The professor gave a derivation of a self similar solution with no velocity at the wall, but I think there is a mistake in it. Please take a look :
Self similar solution condition :
$$BU(x,y)=U(x+dx,\frac{y}{A})\\\\
B=(1+\epsilon')\\\\
\frac{y}{A}=y+\epsilon y$$
through a taylor approximation, he gets a similar solution condition :
$$\frac{\partial U}{\partial x}+\frac{\epsilon}{dx}Y\frac{\partial U}{\partial y} = \frac{\epsilon'}{dx}U$$
with ##\frac{\epsilon}{dx}=\theta## and ##\frac{\epsilon'}{dx}=\alpha##, put in stream function form :
$$\phi_{xy}+\theta Y \phi_{yy}= \alpha \phi_y$$
now take the integral of both sides in order to get a function for ##\phi_x## that can be used to make the stream function as a function of y alone. :
$$\phi_x=v_w-\theta y \phi_y + \phi(\alpha + \theta)-\alpha\phi(y=0)$$
So here is my first question/point of confusion. The professor explains that ##\phi(y=0)=0##. He derived this for a situation with no suction, I am trying to modify it for suction. I think ##\phi(y=0)=-v_w*x## because ##-\phi_x=v##. Is this correct?
Then, we plug I plug it into the stream equation I get :
$$(\alpha+\theta)(\phi_y)^2-[(\alpha+\theta) \phi+v_w-\alpha \phi (y=0)] \phi_{yy}=u_e \frac{\partial u_e}{\partial x} + \vartheta \phi_{yyy}$$
The professor leaves off a ##\theta## from the first term, with ##\phi=0## and ##v_w=0## he gets :
$$\alpha(\phi_y)^2-(\alpha+\theta) \phi \phi_{yy}=u_e \frac{\partial u_e}{\partial x} + \vartheta \phi_{yyy}$$
So... I think he just substituted wrong which is why the first term with ##(\phi_y)^2## does not equal ##(\alpha + \theta)##
Is my equation the correct answer? Also should ##\phi=-v_wx##?