Page 326 - Intro to Tensor Calculus
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                                               Figure 2.5-7. Plane Poiseuille flow


               with u = u(y)and v = w = 0 with boundary values u(0) = u(2`)= 0. The density is constant and ν = µ /%
                                                                                                          ∗
               is the kinematic viscosity.
                                                         2
                                                        d u   p 0
                   (a) Show the equation of fluid motion is ν  +  =0,     u(0) = u(2`)=0
                                                        dy 2   %
                   (b) Find the velocity u = u(y) and find the maximum velocity in the x-direction. (c) Let M denote the
                   mass flow rate across the plane x = x 0 = constant, ,where 0 ≤ y ≤ 2`, and 0 ≤ z ≤ 1.
                                   2     3
                   Show that M =     %p 0 ` . Note that as µ increases, M decreases.
                                                        ∗
                                  3µ ∗
                                                                                          ∂(δcu)
              I 16. The heat equation (or diffusion equation) can be expressed div ( k grad u)+H =  , where c is the
                                                                                            ∂t
                                                                 3
                                                                                                         3
               specific heat [cal/gm C], δ is the volume density [gm/cm ], H is the rate of heat generation [cal/sec cm ], u
               is the temperature [C], k is the thermal conductivity [cal/sec cm C]. Assume constant thermal conductivity,
               volume density and specific heat and express the boundary value problem
                                                           2
                                                          ∂ u     ∂u
                                                        k     = δc  ,  0 <x <L
                                                          ∂x 2    ∂t
                                          u(0,t)=0,    u(L, t)= u 1 ,  u(x, 0) = f(x)
               in a form where all the variables are dimensionless. Assume u 1 is constant.

              I 17. Simplify the Navier-Stokes-Duhem equations using the assumption that there is incompressible flow.

              I 18. (Rayleigh impulsive flow)  The figure 2.5-8 illustrates fluid motion in the plane where y> 0above a
               plate located along the axis where y =0. The plate along y = 0 has zero velocity for all negative time and
               at time t = 0 the plate is given an instantaneous velocity u 0 in the positive x-direction. Assume the physical
               components of the velocity are ~v =(u, v, w) which satisfy u = u(y, t),v = w =0. Assume that the density
               of the fluid is constant, the gradient of the pressure is zero, and the body forces are zero. (a) Show that the
               velocity in the x-direction is governed by the differential equation
                                                       2
                                               ∂u     ∂ u                 µ ∗
                                                   = ν   ,    with    ν =    .
                                                ∂t    ∂y 2                 %
               Assume u satisfies the initial condition u(0,t)= u 0 H(t)where H is the Heaviside step function. Also assume
               there exist a condition at infinity lim y→∞ u(y, t). This latter condition requires a bounded velocity at infinity.
               (b) Use any method to show the velocity is

                                                              y                y
                                         u(y, t)= u 0 − u 0 erf  √  = u 0 erfc  √
                                                            2 νt             2 νt
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