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TABLE OF CONTENTS Pages Symposium 1 - the National Sea ...

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Recirculation systems generally utilize pumps for moving water from <strong>the</strong> tank through<br />

filters or from a sump through a filtering system. Four items are needed to correctly size a<br />

pump:<br />

(1) Desired flow rate (gpm or lpm)<br />

(2) Friction loss from <strong>the</strong> piping and fittings (suction & discharge side)<br />

(3) Vertical distance in which <strong>the</strong> water is to be pumped<br />

(4) Pressure required by filters (1 psi = 2.31 head feet)<br />

Creswell (1993) and Lawson (1997) ga<strong>the</strong>red information on friction losses for selected<br />

valves and fittings as “equivalent length of pipe”. Using this information, <strong>the</strong> total length<br />

of all fittings is added to <strong>the</strong> length of straight pipe needed to give a total length of pipe<br />

which is <strong>the</strong>n used in <strong>the</strong> Hazen-Williams Formula. Major pipe sizes and <strong>the</strong>ir<br />

corresponding friction losses are shown in Table 2. Lawson (1997) recommends using a<br />

C-value of 100 for permanent installations of PVC piping due to future biofouling; new<br />

PVC pipe has a C-value of 150. This calculation along with vertical lift and pressures<br />

required by any filters will give <strong>the</strong> total dynamic head (ft or m). This information along<br />

with <strong>the</strong> desired flow rate and a manufacturers pump graph will present <strong>the</strong> correct size<br />

pump for <strong>the</strong> system.<br />

Table 2.0<br />

Losses are given in head feet per 100’ pipe using <strong>the</strong> Hazen-Williams formula. A C-value<br />

of 130 is used as <strong>the</strong> coefficient using Schd. 40 PVC pipe. Velocities (v) are given in<br />

ft/sec.<br />

0.75 1<br />

Pipe Size (in)<br />

1.5 2 3<br />

Loss v Loss v Loss v Loss v Loss v<br />

GPM<br />

5 10.17 3.63 9.05 2.04<br />

10 36.73 7.26 32.67 4.09 1.26 1.82 0.31 1.02<br />

20 132.58 14.52 69.21 8.17 4.53 3.63 1.12 2.04<br />

30 117.9 12.26 9.61 5.45 2.37 3.06 0.33 1.36<br />

40 178.24 16.34 16.37 7.26 4.03 4.09 0.56 1.82<br />

50 24.75 9.08 6.10 5.11 0.84 2.27<br />

60 34.68 10.89 8.54 6.13 1.19 2.72<br />

70 10.99 7.15 1.58 3.18<br />

80 13.43 8.17 2.02 3.63<br />

90 15.89 9.19 2.51 4.09<br />

100 18.37 10.21 3.05 4.54<br />

110 3.64 4.99<br />

120 4.28 5.45<br />

130 4.97 5.90<br />

140 5.70 6.35<br />

150 6.47 6.81<br />

Note: Generally 5 ft/sec is considered to be safe. Higher velocities may be used in cases where <strong>the</strong><br />

operating characteristics are known and that sudden changes in flow velocity can be controlled.<br />

5

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