Page 32 - Know and Understand Centrifugal Pumps
P. 32

NPSH, Net Positive Suction  Head

        As  a general guide  the NPSHa  should be a minimum  10% above the
        NPSHr or 3 feet above the NPSHr, whichever is greater. Other books
        and experts indicate  that the NPSHa should be  50% greater than  the
        NPSHr,  to avoid  incipient  cavitation.  Again,  be  prepared  for  stricter
        definitions to NPSHr and higher safety margins on NPSHa.

        The NPSHa is in the system. The formula is:
                         NPSHa = Ha + Hs - Hvp - Hf - Hi
        Where:  Ha = Atmospheric head (14.7 psi x 2.31) = 33.9 ft. at sea
                level. See Properties of Water I in this chapter that considers
                atmospheric pressure at different elevations above sea level.
                Hs = Static head in feet (positive or negative) of the fluid level
                in the suction vessel to the pump centerline.
                Hvp = the Vapor head of the fluid expressed in feet. It is a
                hnction of the temperature of the liquid. See Properties of
                Water I1 in this chapter.
                Hf = Friction head or friction losses expressed in feet in the
                suction piping and connections.
                Hi = Inlet head, or the losses expressed in feet that occur in
                the suction throat of the pump up to and including the eye of
                the impeller. These losses would not be registered on a suction
                pressure gauge. They could be insignificant, or as high as 2
                feet. Some pump manufacturers factor them into their new
                pumps, and others don’t. Also, changes occur in maintenance
                that may alter the Hi. If you don’t know the Hi, call it a safety
                factor of 2 feet.
        By observing the system, you can calculate the NPSHa within a one or
        two point  margin. The main  idea is  to be  sure the NPSHa  is  greater
        than the NPSHr of the pump. Remember  that the NPSHa  only deals
        with the suction side of the pump. Let’s go back to that formula:
                        NPSHa = Ha + Hs - Hvp - Hf - Hi

        1.  To determine the Ha, atmospheric head, you only need observe the
           vessel  being  drained  by  the  pump.  Is  it  an  opened,  or  vented
           atmospheric vessel? Or is it a closed and sealed vessel? If the vessel is
           open,  then  we  begin  with  the  atmospheric  pressure  expressed  in
           feet, which is  33.9 feet at sea level. The altitude is important.  The
            atmospheric pressure adds energy to the fluid as it enters the pump.
           For  closed  un-pressurized vessels the  Ha is equal  to the  Hvp and
           they  cancel  themselves.  For  a closed  pressurized  vessel  remember
           that every 10 psia of pressure  on a vessel above the vapor head  of
           the fluid will add 23.1 feet of Ha. To the Ha, we add the Hs.
        2.  The Hs, static head,  is  the static height  in feet observed  from the
            level in the vessel to be drained to the centerline of the pump. If the



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