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Technical Description <br /> during filtration, but precludes any penetration beyond the surface layer. A more efficient media <br /> system incorporating varied media layers is recommended. <br /> The different materials are always different specific gravities and are usually made up of various <br /> sizes of gravel, garnet. sand, and anthracite coal. The denser filter media are placed below the <br /> coarser but less dense coal, thus allowing deeper penetration in the direction of floe and main- <br /> taining a coarse surface layer even after backwash. This filter media design concept is termed <br /> multimedia. <br /> BODS concentrations that are trapped in the suspended solids of the secondary effluent can be <br /> effectively removed in a well-designed tertiary filter; however, standard multimedia filtration has <br /> little or no measurable effect on the removal of soluble BOD, which is generally less than 10 mi- <br /> crons in size. In applications where extreme effluent dedl shinfter the multimedia filtertlters, ultrafil- <br /> red, micro <br /> ters, nanofilters, and even reverse osmosis may <br /> RO, in conjunction with microfilters, is at a state in technological development where it is possi- <br /> ble to remove particulates down filtration <br /> ati0.1 on will ever be cron or 0.00000394 <br /> g000�in4�e wash water trethough atment andikrecy <br /> that the need for this type of f <br /> larnation area except to produce drinking water. <br /> The most important consideration in the sizing of tertiary filters, and one requiring considerable <br /> engineering judgment, is selection of the application rate, which is expressed as gallons per min- <br /> ute applied per square foot of filter surface aiea. <br /> In many cases, the maximum application rate is fixed by a regulatory agency. Some factors that <br /> must be considered in selection of the rate of application include: 1) efficiency of the secondary <br /> filter cycle duration and backwash water production; and 4) <br /> treatment process;2) flow pattern; 3) <br /> capital cost of equipment. <br /> With the Nitro-Raptor system, designed-in plant flow equalization allows <br /> loe'ulttfrom periodic slter flow rate ulec- <br /> rge <br /> tions based on equalized flow rates, which removes the problems that <br /> flows. <br /> With the unique batch design of the Nitro-Raptor secondary process, daily flow patterns (as well <br /> as peak flow rates) are near constant. thus a set schedule can be maintained for backwashing the <br /> filter media during low system flow periods. <br /> COM PUTERIZED/ELECTRONIC/ELECTRICAL-CONTROOSYSTEM <br /> td monitors the operational <br /> The Nitro-Raptor system. control unit provided by and microprocessoroperational <br /> of the entire treatment system with solid-state memory controlling down stream <br /> computerized systems. These systems are capable of monitoring m <br /> uand contrntr with capability m <br /> effluent disposal and reclaimed water systems. This system provides <br /> of <br /> monitoring all remote systems from their Headquarters in Grass Valley, California. They can <br /> coincidentally provide the client with the same information of monitored systems by modem or <br /> Internet Access to 7-H's Web Page. <br /> •17- <br /> 7-H Tecnnical Services Group.Inc. <br />