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The City of Phoenix (City) currently operates four conventional water treatment plants (WTP). The City isupdating its Water Quality Master Plan (WQMP). The initial phase of the WQMP update studyrecommended modifying the current treatment processes to achieve enhanced coagulation (EC)and incorporating additional treatment processes such as granular activated carbon (GAC) filteradsorbers and ozone at all the City WTPs. In order to develop the design and operating criteriafor GAC filter adsorbers and intermediate ozonation (ozonation before filtration), the Cityfunded a pilot study that was performed over a period of seven months from December 2002 toJune 2003. This paper summarizes the key findings of this pilot study.The key objectives of the pilot testing were:can GAC filter adsorbers assist in complying with the Stage-2 D/DBP Rulerequirements;what is the acceptable filter media depth for the GAC filter adsorbers;what are the benefits of backwashing with unchlorinated water; and,what are the benefits of applying ozone prior to the GAC filter adsorbers? To address the above objectives, a pilot facility was constructed and operated adjacent to the Salt River Project's Arizona Canal.This pilot facility had 11 filters; each filter was 3-inches (in) in diameterand 15 feet (ft) tall. Six of the 11 filters received plant settled water (SW) and the rest of the fivefilters received ozonated settled water (OSW). The pilot filters were filled with different mediathat included anthracite (A)/sand (S), bituminous GAC (GAC-B) and lignite GAC (GAC-L).The GACs that were used in the pilot study were of 8x20 mesh size (US Sieve) with an effectivesize of 1.0-1.2 millimeters (mm) and uniformity coefficient of less than 1.5. Virgin reagglomeratedGAC media obtained from a leading national manufacturer was used in this study. The SW and OSW served as the feed waters to the pilot filters. Ozone was applied at a massratio of 0.5 mg of ozone per mg of TOC in the settled water. The average TOC of the SWranged from 1-3 mg/L and therefore the ozone dose ranged from 0.5-1.5 mg/L. At the ozonedose of 0.5-1.5 mg/L, no significant TOC removal was observed. Ozonation lowered theaverage specific ultraviolet absorbance (SUVA) from 1.9 in SW to 1.4 in OSW. The bromideconcentration in SW was between 80 and 110 Au/L. The low ozone dose and the moderateozonation pHs resulted in bromate formation at less than the method detection limit (MDL) of 5micrograms/liter (Au/L).The pilot influents and filtered waters were routinely monitored for field parameters such as pH,turbidity, temperature, ultraviolet (UV) absorbance at 254 nanometers (nm) wavelength, ozoneresidual in OSW and chlorine residual in backwash water. Additionally, samples were collectedand sent to certified laboratories for analysis of TOC, heterotrophic plate counts (HPCs),bromide, bromate, THMs, HAAs and taste and odor (T

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Edition: Vol. - No. Published: 11/02/2003 Number of Pages: 16 File Size: 1 file , 640 KB