• AWWA WQTC69425

AWWA WQTC69425

Temporal Behavior of Post-Filter GAC Adsorbers during THM Formation and Precursor Removal

American Water Works Association , 11/01/2008

Publisher: AWWA

File Format: PDF

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The objective of this study was to evaluate the temporal behavior of post filter adsorbers employing different types of granular activated carbon (GAC) media in the removal of precursors of chlorinated organics and in the formation of disinfection byproducts. The experimental setup was four pilot scale adsorbers, two units with mineral GAC media (CALGON Filtrasorb 300) and another two units with vegetal GAC media (CARBOMAFRA CAG 119). The four adsorbers (F1 through F4) were operated in parallel, with the same empty bed contact time (EBCT) of about 20 minutes. Two of them (F1-CALGON and F2-CARBOMAFRA) were fed with filtered water from a Alto da Boa Vista Water Treatment Plant (ABVWTP) which was ozonated prior to feeding, in order to observe any effects of ozonation on the different adsorbers. The other two adsorbers (F3-CALGON and F4-CARBOMAFRA) were fed with filtered water only. The ozonation system was composed of four column shaped contactors in series. Each column had a hydraulic detention time of 4 minutes. Ozone dosages were applied in the first and second columns of the series. The total ozone dosage was in the range 0.2 through 1.0 mg O3/L and was equally split between columns 1 and 2. Evaluations of precursor removal and disinfection byproduct formation were by means of COT, UV-254 nm determinations and THM formation potential, respectively. The filtered water was from the conventional ABV WTP, whose raw water source is from a highly eutrophic reservoir with a long detention time. COT and UV-254 values for the ozonation system feed water and for adsorbers F3 and F4 were in the ranges 2.0 to 2.5 mg C/L and 0.02 to 0.04 cm-1, respectively. It was observed that ozonation did not affect significantly the COT and UV-254 values. During the first thirty days of post filter adsorber operation, COT removal efficiencies were around 80 % for F1 and F3 (with CALGON GAC media) and around 40 % for F2 and F4 (with CARBOMAFRA GAC media). With sixty days of operation, COT removal efficiencies decreased to 40 % and 20%, respectively and stayed that way during eight months of operation. The mineral GAC media performed better regarding COT and UV-254 removals than the vegetal GAC media. On the other hand, no significant difference in effluent quality was observed regarding adsorbers with the same GAC media type receiving ozonated and non-ozonated filtered water. Thus ozonation did not seem to affect the adsorbing media. Regarding THM formation, adsorbers F1 and F3 presented a better performance than their counterparts (F2 and F4), the same pattern observed regarding COT and U-254 removals. During the first thirty days of adsorber operation, THM reduction efficiencies were about 85 % for F1 and F3 and 50 % for F2 and F4. With eight months of operation, such numbers stabilized around 50 % and 30 %, respectively, with adsorber behavior similar to what happened with regard to COT removal. Continuous, long term operation of the post filter adsorbers will allow us to assess microbiological effects associated to COT removals and THM formation potentials. Includes 7 references, tables, figures.

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