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Theoretical Analysis of the Velocity Gradient

This analysis will be done for both a tube and plate settler. Tube settlers are used in the lab, but plate settlers are used in the Honduras plants, so a model needs to be created to take the differences between the two apparatuses into account.

Calculation of Ratio of Settling Velocity to Particle Velocity

To begin the calculations for the critical velocity, it is important to note that the maximum velocity at the center of a pipe is two times the average velocity and the maximum velocity between two parallel plates is 1.5 times the average velocity.

In order to determine the critical velocity at which floc particles will begin to roll up the tube and into the effluent, we compare the settling velocity with the particle velocity experienced from the velocity gradient.

The settling velocity can be expressed as follows:

insert vt here

The particle velocity expereince as a result of the velocity gradient can be expressed as follows:

insert vparticle here

where phi is the shape factor, equivalent to 45/24

Therefore, the ratio can be expressed as

insert ratio here

When this ratio is greater than one (ie the settling velocity is greater than the velocity experienced by the floc particles in the tube), the flocs will fall back into floc blanket and fail to travel to the effluent. When this ratio is equal to one, the particles will remain stationary in the tube settler. And when the ratio is less than one, the velocity of the particles will exceed the settling velocity and the floc particles will roll up into the effluent, creating a highter turbidity.


Figure 1: The ratio of Sedimentation Velocity to Fluid Velocity vs. Floc Diameter

Figure 1 shows what size floc could be captured by different tube settler diameters. The lines cross the y value of 1 when the sedimentation velocity matches the upflow velocity at the floc diameter.

Calculation of the Minimum Diameter of the Flocs that Settle from the Sedimentation Velocity Equation

Assuming an upward flow velocity of 100 m/day, the diameter of floc that will roll-up was determined by using a root finding algorithm, and the plate settling or tube diameter was plotted versus the minimum floc diameter.


Figure 2: Plate Spacing or Tube Diameter vs. Minimum Floc Diameter

To ensure that flocs in the plate settler don't roll up, we can calculate the minimum diameter of the flocs that settle from the sedimentation velocity equation. Solving for the floc diameter,

insert floc diameter eqtns

insert S equations and explanations?


Figure 3: Floc Diameter vs. Spacing

Figure 3 shows how the linearized equations provide an excellent solution with only tiny divergence for big flocs in small tubes.


Figure 4: Floc Spacing vs. Floc Diameter

Figure 4 graphically displays the linear velocity gradient solutions. The curves are not quite straight on a log log plot. This is due to the quadratic in the velocity profile. We can obtain a very good approximation by using the velocity gradient at the wall and assuming a linear velocity gradient. That assumption makes an analytical solution possible.

insert S eqtn for plate settlers

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