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1 <br /> 11-3 SINGLE-PASS (INTERMITTENT) PACKED-BED FILTERS 725 <br /> b. The velocity for the 0.03-mrn silt is: <br /> vh 800(0.03)2(1) 50 fi+010° T 0.72 m/d <br /> Comment. The deleterious effect of fine silt that may be present in filter sand can be <br /> appreciated from the above computations, even if the actual flow-through were unsatu- <br /> rated.Similarly,the presence of excessive amounts of fine sand can also have deleterious <br /> k effects on the performance of intermittent sand filters. <br /> F <br /> Depth of filter bed. Sand depths have varied from 18 to 48 in (450 to <br /> I 1200 mm) with 24 in (500 mm) being used most commonly. Historically, deeper . <br /> sand beds were used because the top I to 2 in of sand was removed periodically; <br /> however, the added depth is usually not warranted. When shallow 18-in (450-mm) <br /> beds are used, it has been found that the removal of BOD and TSS remains high <br /> while the degree of nitrification that can be achieved is reduced significantly. Addi- <br /> tional discussion on the role of sand depth on treatment efficiency of ISFs may be <br /> found in Peeples et al. (1991). <br /> Hydraulic loading and application rate. Typical hydraulic loading rates <br /> (Lw) for ISFs, based''on peak flow, are in the range from 1 to 2 gal/ft2-d 1(40 to <br /> 80 rnm/d). Although higher hydraulic loading rates have been used, loading rates of <br /> 4 gallft2-d (160 mm/d) resulted in filter clogging for a fine sand (0.29 mm) that was <br /> dosed 24 times/d (Nor, 1991; Darby et al., 1996). Hydraulic loading rates between <br /> " 2tand 6 gal/ft2-d (80 and 240 mm/d) have been used with larger sand sizes. Ex- <br /> perimental loadings of 10 gal/d ft2 (400 mm/d) are being.studied in Oregon (Ball, <br /> 1996). _ <br /> Peak flow is used for.design because the,long-term performance of the filter.h <br /> s dependent'on restricting the amount of organic matter added per do-se.'If the av- <br /> erage flow were used, the amount of organic matter added per dose would exceed <br /> s the recommended value 50 percent of the time. The recommended peaking factor <br /> for ISFs is 2.5. As noted in Chap. 4, in many states, the required design flows are <br /> based on an allowance of 120 to 150 gal/d per bedroom, which in theory accounts <br /> for peak flow. Again, as noted in Chap. 4, bedrooms do not generate wastewater, <br /> people do. Thus, to make the design of ISFs more rational, and to be consistent with <br /> the design of other wastewater management facilities, it is recommended that a per <br /> capita design allowance, based on peak flow, be used for design. For example, if a <br /> per capita allowance of 50 gal/d is used, then the approximate relationship between <br /> the number of bedrooms and the number of persons is as shown in Table 11-9,which <br /> indicates that the use of an allowance is less conservative for one or two bedrooms. <br /> The corresponding allowances for the state of Washington are reported in Table 11-9. i <br /> Although hydraulic loading rates are appropriate for the design of ISFs, a more <br /> appropriate term when considering the performance of ISFs is the hydraulic applica- <br /> tion rate (HAR), expressed in millimeters of.liquid per dose (Emerick et al., 1997). <br /> The HAR is defined as <br /> M Hydraulic loading rate, Ley, m Vd <br /> ` HAR, mm/dose = Dosing frequency, DF, dosed (11-4) <br /> I <br />