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Lamella

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Design Program

The lamella are the plate settlers place in the top section of the sedimentation tank that help floc settle out efficiently. Image Added
 
Image Added
 
 

Lamella Design Program Algorithm

The Lamella Design Program uses four constraints to determine design values, the critical velocity of 10 m/day, the upward velocity at the bottom of the tank, the minimum space between the lamella and the predetermined length of the sedimentation tank. All of these constraints come together to determine the length of the lamella. The minimum spacing between the lamella was determine via laboratory experiments, at spacing closer than 2 cm failure occured. The length of the sedimentation tank is set by the Sedimentation Program. The critical velocity is the rate at which a particle must fall to ensure that it settles out within the plate settlers. If the critical velocity is too large, flocs will not settle out, and will remain in the water sent through the distribution system. However, a small critical velocity comes at the expense of a large cross sectional tank area (so it is not practical to have an unnecessarily small critical velocity). The upward velocity at the bottom of the tank is important for sludge blanket formation, too high and the blanket will form too thin and will not capture particles, too slow and the blanket will either settle out instead of remaining suspended or the shear value in the blanket will be so high that flocs will get broken up in the blanket. Either of these issues would result in the sludge blanket being detrimental to the sedimentation process.

The program starts by determining the height needed for the launders above the lamella. This height needed for the launders is same as the depth of water needed above the lamella. This value is simply a function of leaving enough available headloss through the exit launder about the lamella to keep it properly submerged.

Include Page
H.SedAbove
H.SedAbove

To determine what the how long the lamella need to be, first the active length of the tank and the upward velocity under the lamella must be determined, but both of these values are dependent upon the length of the lamella. Therefore, an iterative loop of the following three equations was created to determine length of the lamella.

The active length of the tank is the total length of the sedimentation tank minus the inactive length of the sedimentation tank found below.

Latex

\large
$$
L.Inactive = L.SedPlate \cdot \cos (AN.SedPlate) + W.InletChannel + W.ExitChannel + 2 \cdot T.ChannelWall
$$


The upward velocity through the lamella:

Latex

\large
$$
V.SedUpActiveBelow = {{Q.Sed} \over {W.Sed \cdot \left( {L.Sed - L.SedInactive} \right)}}
$$


Length of the Lamella:

Latex

\large
$$
L.SedPlateEst = {{B.SedPlateMin \cdot \left( {{{V.SedUpActiveBelow} \over {V.SedCBod}} - 1} \right) + T.SedPlate} \over {\sin \left( {AN.SedPlate} \right) \cdot \cos \left( {AN.SedPlate} \right)}}
$$

The length found in the above loop is an estimated length, The actual lamella length is dependent on the length of the plastic sheeting material that available. Typically this sheeting length is either 8 or 12 feet.

Latex

\large
$$
L.SedPlate = {{L.SedPlateSheet} \over {floor\left( {{{L.SedPlateSheet} \over {L.SedPlateEst}}} \right)}}
$$

From this number the actual upward velocity (V.SedUpActiveBelow) under the lamella and the actual space needed between the lamella are recalculated. The equation for V.SedUpActiveBelow is the same was used above.
The perpendicular, center to center, space between lamella:

Latex

\large
$$
B.SedPlate = {{L.SedPlate \cdot \sin \left( {AN.SedPlate} \right) \cdot \cos \left( {AN.SedPlate} \right) - T.SedPlate} \over {{{V.SedUpActiveBelow} \over {V.SedCBod}} - 1}}
$$

Perpendicular open space between lamella (does not include material thickness):

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S.SedPlate
S.SedPlate

The horizontal distance between lamella; this accounts for the angle of the lamella in the tank:

Latex

\large
$$
B.SedPlateHorizontal = {{B.SedPlate} \over {\sin \left( {AN.SedPlate} \right)}}
$$

Using the available active length in the sedimentation tank and the known length of the lamella, the number of lamella that can fit in the tank can be calculated as follows.
The Number of Lamella:

Latex

\large
$$
N.SedPlates = ceil\left( {{{L.SedActiveMax} \over {B.SedPlateHorizontal}}} \right)
$$

The vertical height taken up by the lamella is simply a function of the lamella length and angle.

Latex

\large
$$
H.SedPlate = L.SedPlate \cdot \cos \left( {AN.SedPlate} \right)
$$

The thickness of the lamella contributes a small but significant dead zone to the tank. Now that the exact number of lamella has been calculated, more accurate values of active tank length, upward velocity, and critical velocity can be found. Calculations for these values are shown below.

Active Length of the Tank:

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L.SedActive
L.SedActive

The Actual Upward Velocity at the Bottom of the Tank:

Include Page
V.SedUp
V.SedUp

The Critical Velocity Up through the Lamella:

Include Page
V.SedC
V.SedC

The height of the water in the sedimentation tank can now be determined. The inletchannel and the lamella and launders coexist in the same top portion the tank. Therefore the water height is the maximum of these two pieces plus space needed for the elements in the bottom of the tank, which include the inlet manifold and drain.

Latex

\large
$$
HW.Sed = \max \left( {\left( {Z.SedSlopes + H.SedFrameWall + H.SedBetween + 2 \cdot outerdiameter(ND.SedPlateFrame) + H.SedPlate + H.SedAbove} \right),\left( {H.SedManifoldPort + H.SedBetween + T.ChannelWall + H.InletChannel} \right)} \right)
$$

where
Image Added

For tanks where there are more than one bay per tank, a wall is constructed to separate bays. This wall has height that comes up to the top of ledge that supports the lamella frame. This was done so that the wall can lend support to the center section of the lamella. The equation used is as follows.

Latex

\large
$$
H.SedBayDivider = Z.SedSlopes + H.SedFrameWall
$$

The inlet manifold is formed by laying concrete plates next to each other. The width of each slope plate is defined by the user. If the length of the sedimentation tank is not equally divided by the width of the plate, there is a leftover space that needs to be filled by a fraction of a plate. This is used for construction purposes. More details of about the inlet manifold can be found on the inlet manifold design page. It should be noted that this calculation could not be done in the inlet manifold program because the size of the inlet channel was needed, and the inlet channel is not defined until after the inlet manifold program.

Latex

\large
$$
{\rm{W}}_{{\rm{SedSlopePlateRemaining}}}  = L_{Sed}  - N_{SedPorts}  \cdot W_{SedSlopePlate}
$$
 Program

h2. Lamella Design Program Inputs and Outputs
[Lamella Program Inputs|Lamella Design Program Inputs]
[Lamella Program Outputs|Lamella Design Program Outputs]

h2. Lamella Design Program Algorithm

The Lamella Design Program uses the triple constraints of the a critical velocity of 10 m/day, an upward velocity at the bottom of the tank of 70 m/day to calculate the space needed between the lamella and the length of the tank set by the [Sedimentation Program|Sedimentation Design Algorithm]. The critical velocity is the rate at which a particle must fall to ensure that it settles out in the plate settlers. If the critical velocity is too large, flocs will not settle out. However a small critical velocity comes at the expense of area (so it is not practical to have an unnecessarily small velocity). The upward velocity at the bottom of the tank is important for sludge blanket formation. If the velocity is too low the blanket will either settle out or the shear value in the blanket will be so high that floc will get broken up in the blanket and thus the sludge blanket could be detrimental to the sedimentation process. 
The program starts by determining the height available for the lamella. After the height available is determined the length of the lamella can be found given an assumed angle of 60deg. Inorder to find the vertical height avaiable for the lamella, first the height of the water needed above the lamella is found.

{include:H.SedAbove}

The distance below the lamella, H.SedBelowSlope, was found in the sedimentation program and based off of the tank fraction given by the user. The vertical height available for the lamella is simply the remainder of the water depth in the sedimentation tank after the slopes and the space needed above the lamella has been accounted for. 

{include:H.SedPlate}

The lenght of the lamella:
{include:L.SedPlate}

The next step is to determine the space between the lamella, needed to satisfy the critical velocity given the tank length found previously. In order to determine the space between the lamella the inactive length of the tank and the upward velocity under the lamella  must be found first. The inactive length of the tank consists of the space occupided by the inlet and exit channels. 
{include:L.SedInactive}

Upward Velocity under the Active Area below the Lamella:
{include:V.SedUpActiveBelow}

Distance from Center to Center between Lamella:
{include:B.SedPlate}

Horizontal Distance Center to Center between Lamella:
{incldue:B.SedPlateHorizontal}

Open Space between Lamella:
{include:S.SedPlate}

The Number of Lamella:
{include:N.SedPlate}

Active Length of the Tank:
{include:L.SedActive}

The Actual Upward Velocity at the Bottom of the Tank:
{include:V.SedUp}

The Critical Velocity Up through the Lamella:
{include:V.SedC}


Critical velocity is the rate at which a particle must fall to ensure that it settles out in the plate settlers. If the critical velocity is too large, flocs will not settle out. However a small critical velocity comes at the expense of area (so it is not practical to have an unnecessarily small velocity). 
 We are designing our tanks to have an upward velocity of 100 m/day. We've found that this is the velocity allows for the formation of a sludge blanket in the bottom of the tank. -Since a portion of the tank's length is rendered unusable due to the sloping of the lamella, the actual length of the tank is greater than the active length.- {color:red}Explain the dual constraints of critical velocity and upflow velocity and detail how both constraints could be met simultaneously or how they could both be set as maximum values. {color}


Sedimentation is a basic step of most traditional water treatment processes. In our plant it comes between flocculation and chlorination. It uses gravity to separate water from the particles - particles settle to the bottom of the tank while the clean water rises to the top. Any particle settling faster than the critical velocity of the tank should settle out. Critical velcoty is a function of the flow rate and setting area of the tank. A particle's settling velcotiy depends on its size and density. Larger particles settle faster and therefore are thereby easier to separate from the clean water. Our design employs plate settlers which lessen the distance a particle must fall in order to settle out. This increases the tanks efficiency.