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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />used. Thi s results in an average daily demand of 185 gpm. A revi ew of <br />relationships between average and peak demand rates was performed. This <br />resulted in estimated peak daily and peak hr)IJr1y rates of aporoxill1ately 550 <br />and 1,200 gom, respectively. <br /> <br />It is necessary to verify that the computer program adequately predicts flows <br />and pressures in the system. Thi s task is greatly hampered by the 1 ack of <br />simultaneous demand and flow measurements. There are few recorded oressure <br />measurements; however, the demand rates at the time these measurements wel'e <br />made are unknown. The best pressure readings available are at the four <br />oressure reducing valves (PRV's) locations as shown in Figure 4.1. These <br />measurements are given in Table 4.1. <br /> <br />=============================================================================== <br /> <br />Table 4.1 <br />Pressure Reducing Valve Measured and Computed Values <br /> <br />PRV Number Measured Pressure (psi) COlllouted Pressure (psi) <br /> Upstream Oownstrea1'1 IJpst,..eam nownstream <br />1 89 40 Cl6 47 <br />2 98 95 71 78* <br />3 no 108 129 108 <br />4 100 100** 104 104 <br /> <br />------------------------------------------------------------------------------- <br />------------------------------------------------------------------------------- <br /> <br />* PRV Closed <br />** Bypass Operating <br /> <br />For the verification of the computer program, the downstream set points of the <br />PRV's were adjusted to cause the same pressure drop as was observed for the <br />measured conditions. There is good agreement between the measured and <br />computed pressures with the exception of PRV Number 2. This valve is located <br />in the far eastern distribution loop on a 2-inch PVC line. The progral'l <br />computed a downstream pressure more than the upstream pressure. Consequently, <br />the valve would be closed. It is believed that the existing valve at this <br />location may be stuck or the pressure measurements are in error. <br /> <br />4-3 <br /> <br />1062c <br />