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SUMMIT EmGINEERING, INC. <br /> Consulting Civil Engineers <br /> July 23, 2001 <br /> Project No. 2001015 <br /> Page B.3 <br /> iii) The pH adjustment will provide a more favorable environment (if necessary) for <br /> the growth of aerobic bacteria in the aerated lagoons; the ammonia will also <br /> serve as a supplemental nutrient in the biological process. The adjustment of the <br /> pH also reduces the chances for emission of hydrogen sulfide odors that can <br /> occur in a low pH environment. <br /> b) Flow measurement—An inline magnetic flow measurement device will be provided to <br /> measure flows from the PW pump stations to the facultative aerated lagoons. <br /> C) Solids removal screen — New motorized rotary drum screens will remove the large solids <br /> from the system at the receiving area and, as a result, reduce the organic biological <br /> loading on and the accumulation of solids in the aerated lagoon system. Solids from the <br /> screening operations will be treated as pomace (refer to solid waste section). <br /> 5. Facultative Aerated Lagoons -- Biological stabilization will occur in the facultative aerated lagoon <br /> (FAL) system consisting of two mechanically aerated ponds in Phase 1 and three mechanically <br /> k aerated ponds in Phase 2. This lagoon system will be large enough to provide a normal <br /> residence time of 64 days at average flow conditions during harvest (see page B.9 and 6.14). For <br /> ultimate process wastewater/rainfall inputs and evaporation/irrigation outputs, refer to the pond <br /> water balance (based on 100 year rainfall and a minimum two foot freeboard) in Enclosure C. <br /> I The total ultimate Phase 2 volume of the lagoon system is approximately 16.735 Mgal (Pond No. <br /> 1: 4.357 Mgal, Pond No. 2: 4.357 Mgal, and Pond No. 3: 8.021 Mgal), with a 2 ft minimum <br /> freeboard. <br /> j Surface mechanical aerators for the aeration cells will be sized to satisfy biochemical oxygen <br /> demand as well as oxygen dispersion requirements. Timer control of the aerators will be <br /> provided to allow operations personnel to adjust aerator operation to changing winery functions <br /> and pond conditions, <br /> i' <br /> i Treatment systems of this type have been utilized at a number of wineries in California and in <br /> other states; locations include: <br /> a <br /> Winery and Location Constructed <br /> Christian Brothers, South St. Helena 1972 <br /> Geyser Peak Winery, Geyserville 1973 <br /> Robert Mondavi Winery, Oakville 1974 <br /> Firestone Winery, Los Olivos 1975 <br /> Chateau St. Jean, Kenwood 1975 <br /> Buena Vista Winery, Sonoma County 1975 <br /> I Jordan Winery, Healdsburg 1976 <br /> Souverain Winery, Geyserville 1978 <br /> Beaulieu Vineyard, Rutherford 1982 <br /> Vichon Winery, Oakville 1982 <br /> Clos du Val Winery, Napa 1983 <br /> Louis M. Martini Winery, Sonoma County 1985 <br /> Ferrari-Carano Winery, Sonoma County 1986 <br /> Joseph Phelps Winery, Napa County 1988 <br /> Mumm Napa Valley, Napa County 1988 <br /> Montinore Vineyards, Washington Co., Oregon 1989 <br />