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<br /> <br />Figure 9: Comparison of Pilot Data and Model Prediction with Full-Scale Prediction <br /> <br />Figure 9 presents the pilot E EO data for 1,4-dioxane from Figure 7 together with the full-scale <br />model of the E EO for 1,4-dioxane in 2 parallel trains of 2- D72AL75 TrojanUVPhox reactors <br />treating 3000 gpm of filtered water by 2-log reduction of 1,4-dioxane. The full-scale design at <br />those peak conditions has an associated E EO of 0.41 kWh/kgal/order at about 18 mg/L of <br />H 2 O 2 as shown in Figure 9. Also shown in Figure 9 is the model result for the pilot-scale <br />system at the 2 gpm operating condition. The improved efficiency of the full-scale system <br />relative to that of the pilot system was explained earlier. This full-scale prediction also <br />accounts for the lamps operating at their end-of-life condition with an allowance for sleeve <br />fouling and a safety factor. <br /> <br /> <br /> <br /> <br /> <br /> 19