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<br />e <br /> <br />e <br /> <br />....-:::=-- <br /> <br />~~~~~~~~;.~~:~::;;;;~~~_t~;~L!.;.;J~.~ <br /> <br />. \ . <br /> <br />Turner Collie <9Braden Inc. <br /> <br />July 29, 1983 <br />Mr. Jerry L. Hodge <br />City of La Porte <br /> <br />Page Two <br /> <br />.,. <br /> <br />At the peak flow rate of 9.375 mgd, the maximum water surface <br />elevation in the headworks will be 25.52 under the bypass <br />condition. This will result in a freeboard of 1.48 feet, <br />which we also consider acceptable. <br /> <br />Our conclusion is that the l8-inch sluice gate in the bypass <br />channel is adequate if the remaining gates are modified to <br />a 36-inch width. During periods when the grit chamber is <br />out of service for cleaning or maintenance, the raw sewage pump <br />station pumps should be controlled so that the flow rate from <br />the station does not exceed the design peak flow of 9.375 mgd <br />(6,500 gpm). The l8-inch sluice gate in the headworks bypass <br />channel is adequate and we recommend that no modifications be <br />made to that gate. <br /> <br />2. WASTE SLUDGE PIPING - check hydraulics of p~p~ng system for <br />transfer of waste sludge between the digester and the thickener <br /> <br />There have been a series of problems with clogging of the waste <br />sludge transfer pipe between the digester and thickener. The <br />pip~. is 8-inch diameter. There is over 200 feet of pipe <br />bet~een the thickener and the digester, and over 350 feet of <br />equivalent length including fittings. The waste sludge is not <br />pumped from the digester to the thickener. The difference in <br />water surface elevations between the digester and the thickener <br />provides the head to overcome friction loss and cause the <br />sludge to flow to the thickener. <br /> <br />We have analyzed the hydraulics of this piping system for a <br />wide range of possible operating conditions. Our analysis <br />indicates that the probable waste sludge flow rate in this <br />pipe is 150 to 200 gpm, with a corresponding range of velocity <br />of 0.96 to 1.28 feet per second in the pipe during wasting <br />periods. Since the wasting operation should not be continuous, <br />ther~ should be no flow at times during the day. In fact, <br />the wasting period should not exceed 2.5 hours at the current <br />plant design rate and 3.8 hours at the future design rate. <br />Under the most favorable operating conditions, our analysis <br />shows that the sludge flow rate will be approximately 300 gpm <br />during wasting periods, with a corresponding velocity of <br />1.9l feet per second. <br /> <br />(2/1 <br /> <br />" <br />