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Kimley»>Horn <br />PARAMETERS AT POE <br />Page 12 <br />Hobart and Oslo provide finished water that is characteristically higher in hardness and alkalinity <br />concentrations for a Floridan membrane plant, this is primarily due to the quality of source water and IRCU's <br />ability to blend. Alkalinity in the finished water provides resistance to pH changes in the system, whether it <br />be from age, temperature, loss of residual, etc. Historically, both WTPs have shown to exhibit a degree of <br />pH fluctuation at POE which operations has primarily attributed to the added turbidity from lime slurry feed <br />or the SCADA's system ability to respond to set point ratios and pH trim functions. <br />IRCU desires to maintain finished water turbidity of approximately 1 ntu and pH of 8.3. Operations has <br />noted difficulty in achieving this target with the lime slurry system, as the pH adjustment after carbonic acid <br />solution system results in variable turbidity values in the finished water. Furthermore, based on differing <br />qualities of the lime slurry that is delivered, operations has had a difficult time "dialing in" a specific flow <br />setpoint and achieving consistent pH and turbidity. Based on operational data, these values can vary from <br />1 - 4 ntu, all while the system is working to achieve the same pH setpoint value. This problem is <br />exacerbated at Hobart, where operations has to essentially run two separate WTP processes with each <br />bank of four NF trains tied to a specific clearwell. To counteract the water quality variation at Hobart, IRCU <br />had implemented caustic feed to supplement the pH and alkalinity increase exhibited by the Cal-flo system, <br />without the added turbidity. This process change was completed in 2016 (during Phase C of the corrosion <br />investigation). Figures 1 and 2 demonstrate a tighter window of pH ranges at Hobart primarily due to the <br />consistent results of caustic feed. Conversely, these figures show that Oslo is able to sustain tighter window <br />for alkalinity and hardness, primarily because the lime slurry system is the sole source of pH adjustment. <br />The following graphs display calcium, alkalinity, and pH values from both facilities at POE: <br />72 <br />