(adsbygoogle = window.adsbygoogle || []).push({}); 1. A conveyor belt with one end immersed in a glycerin tank is used to transport small amounts of glycerin to a second tank. The belt surface is completely smooth, flow is laminar, and the specific weight of the fluid is 60 lbf/ft^3 with the belt velocity equal to 1 ft/s. Determine the volume flow rate and the mass flow rate from the first tank to the second tank per unit foot of width. Take the viscosity to be 0.002 lbf*s/ft^2 and the thickness of liquid (or the height above the conveyor belt) to be 0.04 ft. Assume flow is one-dimensional.

2. Relevant equations

The velocity of the fluid is given by the vector

[tex] \vec { V } =\left\{ u,v,w \right\} \quad [/tex]

Navier-Stokes equation for flow (without the gravitational term):

[tex] \rho \frac { D\vec { V } }{ Dt } =-\nabla P+\mu { \nabla }^{ 2 }\vec { V } [/tex]

Navier-Stokes equation in the x-direction:

[tex] \rho ( \frac { \partial u }{ \partial t } +u\frac { \partial u }{ \partial x } +v\frac { \partial u }{ \partial y } +w\frac { \partial u }{ \partial z } ) = -\frac { \partial P }{ \partial x } + \mu ( \frac { { \partial }^{ 2 }u }{ { { \partial }x }^{ 2 } } + \frac { { \partial }^{ 2 }u }{ { { \partial }y }^{ 2 } } +\frac { { \partial }^{ 2 }u }{ { { \partial }z }^{ 2 } } ) [/tex]

There may be some other equations that I need to use but I don't know for sure.

3. The attempt at a solution

If any of these assumptions are wrong, let me know please. Since it is the conveyor belt that moves the liquid, and the liquid itself is not flowing independent from the belt, the whole left side of the equation becomes 0 since u=0, v=0, and w=0. There is no pressure gradient. In other practice problems in my class, all the laplacian terms have been ignored except for:

[tex] \frac { { \partial }^{ 2 }u }{ { \partial y }^{ 2 } } [/tex]

Though I can't say for sure why (is it because the flow is 1-D and laminar ??). So we're left with:

[tex] 0=\mu \frac { { \partial }^{ 2 }u }{ { \partial y }^{ 2 } } [/tex]

My TA told me that since the viscosity is non-zero, I should work instead with:

[tex] 0= \frac { { \partial }^{ 2 }u }{ { \partial y }^{ 2 } } [/tex]

And solving that differential equation gives me and equation of the form:

[tex] u(y)=Ay+B [/tex]

Since the velocity at u(y=0) must equal the velocity of the belt, the equation becomes:

[tex] u(y)=Ay+{ V }_{ belt } [/tex]

After this I'm stuck, since I don't know what other condition to use to solve for the constant A, or I don't even know if I'm on the right track. Any help would greatly be appreciated.

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# Homework Help: Liquid flow over a conveyor belt

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