Page 113 - Know and Understand Centrifugal Pumps
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Know and Understand Centrifugal Pumps






























       Figure 8-2
       ~~   ~~~~
       Determining the Hs

         Of the four elements of the TDH, the Hs and the Hp (elevation and
         pressure) exist whether the pump is running or not. The Hf and the Hv
         (fiction and velocity losses) can only exist when the pump is running.
         This being the case, we can show the Hs and the Hp on the vertical line
         of the system curve at 0 gpm flow. The Hs is represented as a T on the
         graph below. For example, if the pump has to elevate the liquid 50 feet,
         the Hs is seen in Figure 8-2.



       Determining the Hp

         The Hp also can exist with the pump running or off. We  can represent
         this value with an 0 or oval on the vertical line of the below graph. The
         Hp is added to and stacked on top of the Hs. Let’s say that our system
         is pumping cold water and requires 50 ft of elevation change and 10 psi
         of pressure  change across the system. Now, our pump not only has to
         lift the liquid 50 ft,  but it must also conquer 23 ft of Hp. Remember
         that 10 psi is 23.1 ft of Hp:

                10 psi x 2.31
         Hp  =
                    SP- gr.
         Here is the system curve showing Hs and Hp (Figure 8-3).
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