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The flow through the alum doser exit tubing was determined given user-defined parameters for the dimensions of the alum stock tank, such as height of tank (and thus, height of alum level) and diameter of exit orifice (and thus, diameter for the attached plastic tubing). These calculations were completed by simplifying the system to a "hole-in-the-bucket" situation.
Next, using the previously determined flow through the exit tubing, the flow through each of the one orifice plates plate can be easily determined. The calculations for flow assumes that flow through the tube was constant and neglects the effect of gravity on the flow. We assumed that the flow was fast enough to support this neglection.
Then, Total head loss through both the tubing and orifice plates are were calculated given user input for width and number of orifice plates. These calculations utilize the fluids functions found at the top of this page. Essentially, the head loss through one orifice plate was determined. The total head loss through the plates was then found by multiplying the number of plates by the head loss through one plate only. It should be noted that the head loss through these plates are purely cause by shear forces and thus experience major losses only.
Head loss through the external tubing was then calculated given user input for the the desired length of the tubing. The calculations were similar to those above. The plates along with the length of the desired tubing. This total head loss through the system is then can be defined as the summation of the head loss through the orifices plates and the head loss through the wider, encompassing tubing.
Head Loss Through Orifice Plates:
Head Loss Through Tubing: 
Using this information, the necessary flow of alum from the doser based on dimensions given above is determined. Using a stock required dose concentration of 1.5 mg/L in the untreated water, the necessary stock concentration is found as welllocated in the alum doser can be calculated.
The following section calculates the flow of alum given varying alum stock heights (of 5 inches to 25 inches). The final graph depicts results showing that if alum stock height varies greatly, the flow remains generally within the acceptable flow error. This error stems from the fact that we are not using alum for flocculation. Flocculation requires precision whereas merely dosing for improved performance leaves room for some error.
These results prove that the design will not work well with our point-of-use unit. By playing with the dimensions of the tubing, orifice plates, alum doser itself, and more, the lowest average flow we could obtain was around 12 mL/s which is extremely high for our desired system. Given this value, 1,037 L of alum stock would be used per day.