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                                          HVAC Pump Performance

                                                            HVAC Pump Performance  161

                           P   static head of water level above the pump impeller (This
                            s
                               is negative if water level is below the impeller.)
                          P   vapor pressure of water, in feet, at operating temperature
                           vp
                               (see Tables 2.3 and 2.4)
                           P   friction of suction pipe, fittings, and valves, in feet of head
                            f
                      Equation 6.8 can be used for higher temperatures and elevations.
                      Assume the following:
                    1. The maximum cooling tower water temperature is 95°F, so P
                                                                                 vp
                       1.9 ft of vapor pressure. From Table 2.3.
                    2. The cooling tower sump is above the pump impeller, and P   5 ft.
                                                                             s
                    3. The installation altitude is 1000 ft; From Table 2.1, the atmospheric
                       pressure, P = 32.8 ft.
                                 a
                    4. The friction loss of the suction pipe, fittings, and valves P is 6 ft.
                                                                              f
                       Thus

                                   NPSHA   32.8   5   1.9   6   29.9 ft
                      Any pump handling this water must have an NPSHR of less than
                    29.9 ft at any possible flow through the pump.
                      Warning. Calculation of NPSHA for a cooling tower should be made
                    at the maximum possible operating water temperature in the tower, not
                    the design water temperature.



                    6.5.2 Air entrainment and vortexing
                    A companion to cavitation is air entrainment in the suction of cen-
                    trifugal pumps. Air can enter the water system at several points, as
                    shown in Fig. 6.16a. The effect of air entrainment on pump perfor-
                    mance is described in Fig. 6.16b; it indicates the drastic reduction in
                    both head and capacity when air is present. Every effort must be
                    made to ensure that the water in a pump is free of air.
                      Air entrainment is often confused with cavitation when drawing
                    water from a tank. It is thought that air entrainment cannot happen
                    when a tank of water is 10 to 15 ft deep. Air entrainment can occur eas-
                    ily when water is taken from a free surface of water regardless of the
                    depth of the water. Figure 6.17 describes the air entrainment that can
                    occur if water is not removed properly from an open tank. As shown
                    in Fig. 6.17a, a small whirlpool occurs on the surface, and this deep-
                    ens into a vortex that will extend down to the water outlet from the
                    tank, and finally, air will pass into the impeller of the pump, causing




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