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                                          HVAC Pump Performance

                    164   HVAC Pumps and Their Performance

                    bottom inlet, as shown in Fig. 6.17b; a side inlet can be corrected by
                    placing an antivortexing plate above the inlet (Fig. 6.17c). On shallow
                    cooling tower sumps, if vortexing persists, it may be necessary to in-
                    stall a slotted vortex breaking tube, as shown in Fig. 6.18d. As an al-
                    ternative, an elbow can be installed on the suction connection of a
                    side inlet and pointed downward, as shown in Fig. 6.17e. If vortexing
                    still occurs, a square plate can be installed on the suction of the elbow.
                    Vortex-breaking devices must be designed to avoid substantial addi-
                    tional friction losses. Normally, the friction loss of an entrance from a
                                                   2
                    tank is equal to about 0.5   V /2g, where V is the velocity of the
                    water in the entering pipe. The vortex-breaking device should not
                    increase this entrance loss if possible.
                      A simple method to determine if vortexing is occurring is to place
                    mats or rafts on the water surface above the inlet from the tank. This
                    prevents the vortex from forming and can be done without draining
                    the tank.
                      Vortexing should not occur in HVAC tanks and sumps. The precau-
                    tions are so simple that the design of these tanks and sumps should
                    always accommodate them.


                    6.5.3 Submergence of pumps in wet pits or
                    open tanks
                    Pumps installed in a tank, such as vertical turbine pumps, have a
                    specific submergence requirement. The submergence, or distance
                    above the inlet bell of such a pump, must be great enough to ensure
                    that the friction loss of the water passing through the bell and enter-
                    ing the pump is made up by the static height of the water over the
                    suction bell. This height is determined by whether the suction of the
                    pump is or is not equipped with a suction strainer. Most manufactur-
                    ers of axial-flow pumps have adequate data on submergence and
                    clearance from the bottom of the tank for the water system designer;
                    their recommendations should always be followed. Table 6.1 describes


                    TABLE 6.1 Typical Submergences for Vertical Turbine Pumps (for Operation at
                    1750 rev/min)
                     Bowl size, in   Submergence, in    Bowl size, in   Submergence, in
                         04               07                13               23
                         06               11                14               30
                         08               12                15               32
                         10               16                16               36
                         11               20                18               36
                         12               24                20               42





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