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ChE441 Problem Set 3 Solutions

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PROBLEM SET #3 SOLUTIONS 3B.11 Radial flow between two coaxial cylinders

Consider an incompressible fluid, at constant temperature flowing radially between two porous cylindrical shells with inner and outer radii κR and R.

(a) Show that the equation of continuity leads to vr = C/r, where C is a constant. Solution

Assume that vz =vθ =0and that the flow is steady. Continuity equation in cylindrical coordinates:

(

)

1

( )

( )

0 1 = ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ z r v z v r rv r r t ρ θ ρ ρ ρ θ

Eliminate time, v and θ v terms to obtain: z

(

)

0 1 = ∂ ∂ r rv r r ρ Integrate to obtain: = r rv constant

(b) Simplify the components of the equation of motion to obtain the following expressions for the modified pressure distribution:

0 , 0 , = = − = dz dP d dP dr dv v dr dP r r θ ρ Solution BSL page 848 equation B.6-4.

( )

r r r r r z r r r r v g r z v v r rv r r r r P r v z v v v r v r v v t v ρ θ θ µ θ ρ θ θ θ+      ∂ ∂ − ∂ ∂ + ∂ ∂ +       ∂ ∂ ∂ ∂ + ∂ ∂ − =     − ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ 2 2 2 2 2 2 2 2 1 1

Assume steady flow with vθ =vz =0, no viscous flow as in part (a):

r P r v v r r ∂ − = ∂ ∂ ρ

(c) Integrate the expression for dP/dr above to get

[

]

              − = − 2 2 1 ) ( 2 1 ) ( ) ( r R R v R P r P ρ r Solution r P r v v r r ∂ − = ∂ ∂ ρ

Integrate between R and r:

(

)

     − =         − − =         − − = − = − 2 2 22 2 2 2 2 2 1 2 1 2 2 2 2 R r r v v v r v v v v P P r R r r r r R r r r r R R R ρ ρ ρ ρ ρ

Note: from (a) rvr =constant, so r2vr2 =C2 and 2 2 2 2 R r v v R R r r =

(2)

Direction of flow r

R mR

Radial Flow Between Concentric Spheres

Consider an isothermal, incompressible fluid flowing radially between two concentric porous spherical shells. Assume steady laminar flow with vr = vr(r). Note that the velocity

is not assumed zero at the solid surfaces. See the figure below.

(a) Show by use of the equation of continuity that r2vr = C, where C is a constant.

Solution

Begin with the equation of Continuity in Spherical Coordinates:

(

ρ

)

θ θ

(

ρ θ θ

)

θ φ

( )

ρ φ ρ v r v r v r r r t r ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ sin 1 sin sin 1 1 2 2 =0

Assume radial flow, so that vθ =0=vφ.

( )

0 1 2 2 ∂ = ∂ r v r r r

So that after integration:

=

r

v r2

Constant

(b) Show by the use of the equations of motion that the pressure distribution in this

system is described by the equations:

φ ρ φ θ g p r ∂ = ∂ sin 1 θ ρ θ g p r ∂ = ∂ 1

( )

r r r gr r v v v r r r r p ρ ρ µ + ∂ ∂ − ∂ ∂ = ∂ ∂ 2 2 2 2

(3)

Solution

Begin with the equation of motion in spherical coordinates (BSL equation B.6-7 page 848). r-component

( )

r r r r r r r r r g v r v r v r r r r p r v v v r v v r v r v v t v ρ φ θ θ θ θ θ µ φ θ θ ρ θ φ θ φ +                   ∂ ∂ +       ∂ ∂ ∂ ∂ + ∂ ∂ + ∂ ∂ − =     − − ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ 2 2 2 2 2 2 2 2 2 2 2 sin 1 sin sin 1 1 sin

Assuming steady state and that vφ =0=vθ, then the above equation reduces to:

( )

r r r r r v g r r r p r v v µ ρ ρ +      ∂ ∂ + ∂ ∂ − =       ∂ ∂ 2 2 2 2 1 Rearrange:

( )

r r r r g r v v v r r r r p ρ ρ µ + ∂ ∂ − ∂ ∂ = ∂ ∂ 2 2 2 2 θ-component θ φ θ θ θ φ θ θ φ θ θ θ θ ρ φ θ θ θ φ θ θ θ θ θ µ θ θ φ θ θ ρ g v r v r v r v r r v r r r p r r v r v v v r v v r v r v v t v r r r +                         ∂ ∂ − ∂ ∂ + ∂ ∂ +       ∂ ∂ ∂ ∂ +       ∂ ∂ ∂ ∂ + ∂ ∂ − =     − + ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ 2 2 2 2 2 2 2 2 2 2 2 sin cos 2 2 sin 1 sin ( sin 1 1 1 1 cot sin Since vφ =0=vθ, θ ρ θ g p r ∂ + ∂ − = 1 0 Rearranging, θ ρ θ g p r∂ = ∂ 1

(4)

φ-component θ θ φ φ φ φ θ φ φ φ φ θ φ φ ρ φ θ θ φ θ φ θ θ θ θ θ µ φ θ θ φ θ θ ρ g v r v r v r v r r v r r r p r r v v r v v v r v v r v r v v t v r r r +                           ∂ ∂ − ∂ ∂ + ∂ ∂ +       ∂ ∂ ∂ ∂ +     ∂ ∂ ∂ ∂ + ∂ ∂ − =     + ∂ ∂ + ∂ ∂ + ∂ ∂ + ∂ ∂ 2 2 2 2 2 2 2 2 2 2 sin cos 2 sin 2 sin 1 sin ( sin 1 1 1 sin 1 cot sin Since vφ =0=vθ, φ ρ φ θ g p r ∂ + ∂ − = sin 1 0 Rearranging, θ

ρ

θ

g

p

rs

=

1

(c) Show that the radial pressure distribution may be expressed in terms of the quantity

P as:               − = − = 4 2 1 2 1 r R v P P R r r R ρ Solution

Begin with equations from results of part (b),

( )

r r r r g r v v v r r r r p µ ρ +ρ ∂ ∂ − ∂ ∂ = ∂ ∂ 2 2 2 2 (1) using, θ ρ φ gφrsin p = ∂ ∂ (2) r g p θ ρ θ = ∂ ∂ (3) gr p gr p P= +ρ cosθ = +ρ θ ρ cosg r p r P + ∂ ∂ = ∂ ∂ θ ρ θ θ grsin p P ∂ ∂ = ∂ ∂ Substitute (3) 0 sin = − = ∂ ∂ ρ ρ θ θ gθr gr P so PP(θ)

(5)

( )

ρ ρ µ

( )

ρ ρ θ ρ θ µ

θ

ρ cos 2 2 cos cos

2 2 2 2 2 2 g g r v v v r r r g r v v v r r r g r p r P r r r r r r r + − ∂ − ∂ ∂ = + ∂ ∂ − ∂ ∂ = + ∂ ∂ = ∂ ∂

( )

2 2 2 2 2 2 r v r v v v r r r r P r r r r ρ µ µ ∂ ∂ − ∂ ∂ = ∂ ∂ Since r vr = 2 Constant, then

( )

0 2 = ∂ ∂ r v r r

( )

( )

5 2 2 2 2 2 2 2 2 2 2 r C r v v v r v r r P r r r r ρ ρ ρ µ µ + = = = ∂

where C is the constant from part (a)

dr r C dP 5 2 2ρ =

= r R P P r dr C dP r 5 2 2ρ       = − 2 14 14 4 2 R r C P P r ρ Substitute C=R2vr and C2=R4vr2

( )

( )

             − =       = − 4 4 2 4 4 4 2 4 1 1 2 1 1 1 2 1 r R R v R R r v R P P r ρ r ρ r And thus,               − = − = 4 2 1 2 1 r R v P P R r r R ρ

(d) Please write expressions for τrr, τθθ, τϕϕ, τrθ, τrϕ, and τθϕ for this system.

Solution

(

)

 − ∂  ∂ ∂ − =     ∂ ∂ − = r v r v v r vr r r rr 3 2 2 3 2 2 µ µ τ

Next, utilize the result of (a) to obtain:

( )

     ∂ ∂ − ∂ ∂ − r v r r r vr r rr 2 2 3 2 2 µ τ Since r2vr = Constant,    − − = r vr rr 2µ 2 τ r vr rr µ τ =4

(

)

 − ∂       + ∂ ∂ − =          + ∂ ∂ − = r v r v v r v r v v r r r r 3 2 1 2 3 2 1 2 θ µ θ µ τ θ θ θθ

(6)

Using the same strategy as above,

( )

( )

+

=

+

=

r

v

r

r

r

v

v

r

r

v

r

r

r

v

v

r

r r r r 2 2 2 2

3

2

2

2

3

2

1

2

θ

µ

θ

µ

τ

θ θ θθ r vr µ τθθ =−2

(

)

( )

     ∂ ∂ − − =       • ∇ −     + + ∂ ∂ − = r v r r r v v r v r v v r r r r 2 2 3 2 2 3 2 cot sin 1 2 θ µ φ θ µ τ φ θ φφ r vr µ τφφ =−2

Since we have symmetric flow,

0 = = = φ θφ θ τ τ τr r

References

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