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terraces,each.45 m long x 4.5 m wide and slopes Temperature also has an effect on runoff BOD <br /> of 2, 4 and 8% (Peters et al. 1981). Detention times concentrations. Martel et al. (1980) found that <br /> times were measured using the same procedure BOD concentrations in the runoff exceeded 30 mg/L <br /> developed at CRREL. �atsoll temperatures at or below 4°C. However, <br /> The second site is located indoors at the Univer- temperature effects shou not e a significant <br /> sity of California at Davis. Each laboratory scale problem at full-scale facilities if wastewater is <br /> model terrace is 6 m long x 1.5 m wide and set at stored during the winter. In this study, temperature <br /> a 4%slope (Smith et al. 1980). Deionized water effects were nullified by selecting performance data <br /> was used as the tracer and a response curve was obtained during the growing season only (April <br /> developed by measuring specific conductance. through October). <br /> A combined total of 40 detention time measure- The experimental data obtained at CRREL and <br /> ments were taken at both sites. Measured detention the University of California, Davis (Fig. 6) indicate <br /> times are shown in Table 3 along with the predicted that BOD removal can be expressed as a first-order <br /> detention times calculated from eq 13. The average equation in the form <br /> difference between predicted and measured deten- <br /> tion times was only 8 minutes. In most cases the <br /> measured detention time was longer than predicted, Percent removal= (1 -A e kT) 100. (14) <br /> which allows an extra margin of safety in the design. <br /> The coefficients and k,obtained by a least- <br /> In a Student's t distribution, the difference between I <br /> measured and predicted detention time was not squares fit to the data,were 0.52 and 0.03 min { <br /> significant at the 95% level. respectively. The coefficient k is the average kinetic <br /> Although the average difference between pre- rate constant. The coefficientA can be interpreted <br /> dicted and measured detention time was not signifi- as the non-settleable fraction of BOD in the applied <br /> cant, individual differences were considerable. This wastewater while the remaining settleable fraction <br /> is understandable, considering the variability of the (0.48) is removed during the first few meters or <br /> surface microtopography from one terrace to another. minutes after wastewater is applied. This conclusion <br /> Construction techniques, patterns of vegetative is supported by the BOD vs downslope distance data <br /> growth and harvesting operations are also factors shown in Figure 7 where 44%of the BOD was re- <br /> which can change the hydraulic detention time. moved <br /> ved within the first 5 m. <br /> TSS removal <br /> KINETICS Total suspended solid (TSS) removal v�ragee <br /> detention time from the CRREL site is shown in <br /> Kinetic relationships describing removal of BOD, ig�ure .Thflat slope of the estimated line of <br /> TSS, NH3-N and total P were developed by taking <br /> best fit indicates that TSS removal changed little <br /> several detention time measurements during each over the range of detention times tested.( oma r example, <br /> application period. The average detention time at a detention time of 20 minutes,TSS removal was <br /> (T)was then calculated along with the average per- .....86%. A three-fold increase in detention time (60 <br /> cent removal on a mass basis for each constituent. min) only increased removal by 6%. <br /> All raw data used in this development can be found The high solids removal efficiency of the overland i <br /> in Appendix A. flow process is due to the shallow depth of water <br /> and the long travel distance to the end of the terrace. <br /> BOD removal Even minute particles with slow settling velocities <br /> BOD is removed by sedimentation,filtration and are able to settle out before reaching the collection <br /> biological oxidation (U.S. EPA 1977). The first ditch. Also, grass and vegetative litter help to entrap <br /> two mechanisms are responsible for removing par- and filter out particles. Data plotted in Figure 7 <br /> ticulate BOD. The soluble BOD is oxidized by mi- indicate that most of the suspended solids were re- <br /> croorganisms which are probably similar to the moved within the first 5 m. <br /> attached biomass found in trickling filters. However, Because of rapid settling,a buildup of solids is <br /> some soluble organic compounds are released from apparent at the top of most overland flow terraces <br /> the plant-soil system,and as a result,runoff ROD which receive raw or primary wastewater. At the <br /> concentrations below to 5 m L cannot be ex- site, so sition was eav <br /> s epoy enough in <br /> petted (Overcash et al. 1976). some spots to smother grass growth. Similar condi- <br /> 7 <br />