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Wnier Treatment Plunt Production Study <br />"Enhanced Coagulation" mode, increasing the cost of operation and possibiy <br />making turbidiiy removal more difficult. The purpose of enhanced coagulation is to <br />achieve higher percentages of TOC removal and reduce disinfection byproducts such <br />as TTHMs and HAAs. <br />The second area of the study was preozonation evaluation, assessing the potential <br />following benefits in water treatrnent: <br />6 Improves turbidity removal <br />inno ,ot ~ iAp~-oar~-:~:. <br />~;D <br />FIcuxe 7•i <br />~ <br /> <br />~ <br />~ <br /> <br />~ _ <br />& [mproves color removal <br />♦ Improves taste and odor reduction <br />~ Controls chlorination byproducts' such as TTHMs and HAAs <br />~ Stronger disinfectant than other commonly used disinfectants <br />The purpose of this report was to present the final results of enhanced coagulation <br />and ozonation pilot testing for all four quarters of testing. <br />SUMMARY OF TESTING RESULTS <br />Enhanced Coagulation Testing <br />lb The STEP 1 TOC removal requirement was 35% for a(I quarters of testing. <br />The STEP 2 removal requirement by ferric sulfate in the second quarter <br />(16.5%) is based on the TOC removal vs. coagulant dose cunve. <br />♦ Of the eight exception criteria, only the raw water SWA excepfion was met <br />in the first two quarters at the Grapevine WfP. Othenvise, the plant was <br />required to meet either a STEP 1 or STEP 2 TOC removal requirement. <br />♦ The enhanced coagulation testing shows that the City was able to meet the <br />STEP 1 TOC removal requirement in the last two quarters by adding from 60 <br />mg/L to 95 mg/L of alum. In the first huo quarters, Alum was unable to meet <br />either the STEP 1 or the STEP 2 removal requirements. A high dose (95 <br />mg/L) of ferric sulfate met the STEP 1 removal requirement in the first <br />quarter, and a ferric sulfate dose of 38 mg/L. met the STEP 2 removal <br />Ii:LLSFI-NIGHOLS <br />rt, r c..w.ie. <br />W.t.. T.ue...e Pl..t <br />