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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 />The sequence of procedures used was to determine inlet, culvert, and <br />flume capacities, and model stormwater runoff with diversions from the <br />surface. HEC-2 models take the balance of flow not diverted to the <br />fl umes. <br /> <br />1. Appendix "0", Culvert Capacities <br /> <br />Culverts have substantial slope, and unlike flumes, do not have <br />additional inflow or intermediate openings to the surface. Inlet <br />control was assumed to govern. <br /> <br />Flume capacities were analyzed for more than just inlet control. <br />Hydraulic gradients are calculated to determine overall maximum <br />capacity, which is the lessor of pipe or inlet capacity. <br /> <br />2. Appendix "E", Inlet Capacities <br /> <br />Inlet capacities were discussed in the Criteria Section. However, <br />it may be beneficial to note here that the HEC-12 procedures were <br />based on grate types, flow velocity, percent of flow over the <br />grate, splash over velocity, and length of grate. The method is <br />very suitable to existing conditions. <br /> <br />9 <br /> <br /> <br />3. Appendix "F", Flume Capacities <br /> <br />Kinematic: viscosity of water at 62'F is 1.185 x 10.5 ft2/sec. This <br />would likely be a minimum viscosity for stormwater. As a maximum <br />amount, 38.6 x 10.5/ft2 sec. is assumed, which is the value for <br />linseed oil. Sediment laden stormwater is assumed to be between <br />these two (2) extremes. It is apparent from the photographs of <br />stormwater flow in the street in Blackhawk, which has similar <br />slopes and watershed conditions, that the flow has low viscosity <br />and would be within the above range. (See photographs in Appendix <br />"F", pages F-4 and F-5.) <br /> <br />Roughness is determined by using roughness depth divided by pipe <br />size. Using the above values and the Darcy equation, and limiting <br />total headloss in the flumes to the average flume slope to <br />approximate a non-surcharged condition, it can be seen from the <br />Moody diagram that the range between water and linseed oil for the <br />given conditions lies on a flat portion of the friction curve <br />entirely in the complete turbulence range for CMP and rock flumes <br />and nearly all in the complete turbulence range for concrete. <br />Accordingly, use of either viscosity produces the same friction <br />value in the Darcy equation for a given headloss. The Darcy <br />equation can then be equated to Manning's equation, setting <br />headlosses as equal, and an equivalent turbulence and viscosity <br />adjusted "n" value in Manning's equation can be determined. This <br />procedure resulted in a minimum CMP and rock wall Un" value of <br />0.027, which is less than the 0.035 value used in analysis. The <br />turbul ence and vi scosity adjusted "n" val ue for concrete was <br />determined to be 0.013, which is less than the 0.025 value used in <br />the Nevada flume and 0.030 value used in the Eureka flume. The <br />conservative "n" values are selected to account for additional flow <br />quantity due to sediment, minor blockage, other unknowns in <br />