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select a valid loading rate within such a wide range. between detention time and removal of biochemical <br /> Also,little information is given on how other var- oxygen demand (BOD), total suspended solids (TSS), <br /> iables such as terrace length and slope can affect ammonia (NH3-N) and total phosphorus (total P). <br /> performance. Thus,a more comprehensive and With these relationships, the designer can determine <br /> rational design procedure, which takes these factors the detention times needed to achieve the desired <br /> into account, is needed to assure that discharge removal efficiency. <br /> requirements are met. The specific objectives of this study were to <br /> The new design procedure developed in this 1. Develop a method which can be used to pre- <br /> report is based on reactor kinetics, a concept dict the hydraulic detention time. <br /> familiar to most environmental engineers. In the 2. Determine the removal kinetics for BOD,TSS, <br /> case of overland flow, the reactor is the soil surface NH3-N and total P. <br /> where v rriious physical, bio 'cal and chemical 3. Validate the detention time and kinetic re- <br /> reactions take place. As in conventional process lationships using data from other systems. <br /> design, the controlling parameter is detention time. 4. Provide an example using the new design pro- <br /> For overland flow,detention time is the average cedure. <br /> time a unit volume of water takes to travel from <br /> the toD to the bottom o t e terrace. The desired Scope <br /> level of treatment can be achieve y controlling Data used in the development of the design pro- <br /> the length of time that wastewater remains in con- cedure were obtained from the CRREL overland <br /> tact with the soil surface. With this approach, flow test site in Hanover,New Hampshire,during <br /> overland flow systems can be constructed for a the 1978 and 1979 growing seasons (April through <br /> wide range of site conditions as long as detention October). All the kinetic relationships were Bevel- <br /> time requirements are met. This would significantly oped using primary effluent;use of this procedure <br /> reduce site preparation costs. for design of overland flow systems receiving a <br /> secondary or lagoon effluent will be discussed later <br /> Objectives in the report. <br /> A design procedure based on detention time re- The hydraulic detention time relationship devel- <br /> quires knowledge of two basic relationships. First oped at CRREL was validated using data from the <br /> is the hydraulic relationship among application Utica, Mississippi,overland flow site (Peters et al. <br /> rate,site characteristics an etention time. With 1981) and the pilot scale system at the University <br /> t_Fiis relationship the designer can determine the of California, Davis (Smith et al. 1980).. Data from <br /> application rate needed to satisfy detention time several other domestic and foreign overland flow <br /> requirements. Second is the kinetic relationship systems were used to validate the kinetic relationships. <br /> B.e m (29)/ I---2.9m (9.i�) <br /> .r,..�./I, ..... .,, .....\. ....mal-� <br /> .._... .. Seq lion / BeStlon •9e bion <br /> �` ' Bar face Floes _ <br /> 1t <br /> meBasin <br /> ���'s Primary <br /> irk., 4. �Jn l� _ ..���.-.vd ,gyp ,T/vl-a ,• Naslevcler <br /> Runoff • <br /> Figure 2. Schematic of CRREL overland flow test site. <br /> 2 <br />