homework transport phenomena

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TRANSPORT PHENOMENA Homework (30% exam I) 1. Assume that for a certain steady, two-dimensional flow in a región defined by ≥0 and ≥0, one velocity component is given by: (, ) = Where and are constants. A. Assuming that the fluid is incompressibe and that (, 0) = 0, determine (, ). B. For what values of will the flow be irrotational? C. For what values of can the Navier-Stokes equation be satisfied? For those cases determine the dynamic pressure, (, ), assuming (0,0) = 0 . 2. Figure shows an example of a system with a gas-liquid interface of unknown shape, consisting of a liquid in an open container of radius that is rotated at an angular velocity . If the container is rotated long enough, a steady state is reached in which the liquid is in rigid-body rotation. It is desired to determine the steady-state interfase height, ℎ(), assuming that the ambient air is at a constant pressure, 0 . The viscous stress vanishes for rigid-body rotation. The effects of surface tension will be neglected. Show that interface height is (¿Newtonian or non-Newtonian fluid?): ℎ() = ℎ + 2 2 2 [( ) 2 1 2 ] Where ℎ ≡ /( 2 ) is the liquid height under static conditions. is the volume of fluid.

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  • TRANSPORT PHENOMENA

    Homework (30% exam I)

    1. Assume that for a certain steady, two-dimensional flow in a regin defined by 0 and 0, one velocity component is given by:

    (, ) =

    Where and are constants.

    A. Assuming that the fluid is incompressibe and that (, 0) = 0, determine (, ).

    B. For what values of will the flow be irrotational?

    C. For what values of can the Navier-Stokes equation be satisfied? For those cases determine the dynamic pressure, (, ), assuming (0,0) = 0.

    2. Figure shows an example of a system with a gas-liquid interface of unknown shape, consisting of

    a liquid in an open container of radius that is rotated at an angular velocity . If the container is rotated long enough, a steady state is reached in which the liquid is in rigid-body rotation. It is

    desired to determine the steady-state interfase height, (), assuming that the ambient air is at a constant pressure, 0. The viscous stress vanishes for rigid-body rotation. The effects of surface tension will be neglected.

    Show that interface height is (Newtonian or non-Newtonian fluid?):

    () = +22

    2[(

    )2

    1

    2]

    Where /(2) is the liquid height under static conditions. is the volume of fluid.

  • 3. A flat plate at = 0 is in contact with a Newtonian fluid, initially at rest, which occupies the space > 0. At = 0 the place is suddenly set in motion in the direction at a velocity , and that plate velocity is maintained indefinitely. This problema may be viewed, for example, as representing the

    early time (or penetration) phase in the start-up of a Couette viscometer.

    A. Show that the non-dimensional formulation of the problem is (analyze the Navier-Stokes

    equation):

    2

    2+ 2

    = 0

    Where = / and =

    4. Moreover is a function of .

    B. Solve the ordinary differential equation and determine the fluid velocity as a function of time

    and position. For the mathematical solution, associate the boundary conditions with and .

    C. Plot the velocity profile for different times. Assume that the kinematic viscosity () is equal to 1 and is very small.