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1.
Water Res ; 46(10): 3177-88, 2012 Jun 15.
Article in English | MEDLINE | ID: mdl-22525456

ABSTRACT

Electrocoagulation (EC) and chemical coagulation (CC) are employed in water treatment for particle removal. Although both are used for similar purposes, they differ in their dosing method - in EC the coagulant is added by electrolytic oxidation of an appropriate anode material, while in CC dissolution of a chemical coagulant is used. These different methods in fact induce different chemical environments, which should impact coagulation/flocculation mechanisms and subsequent floc formation. Hence, the process implications when choosing which to apply should be significant. This study elucidates differences in coagulation/flocculation mechanisms in EC versus CC and their subsequent effect on floc growth kinetics and structural evolution. A buffered kaolin suspension served as a representative solution that underwent EC and CC by applying aluminum via additive dosing regime in batch mode. In EC an aluminum anode generated the active species while in CC, commercial alum was used. Aluminum equivalent doses were applied, at initial pH values of 5, 6.5 and 8, while samples were taken over pre-determined time intervals, and analyzed for pH, particle size distribution, ζ potential, and structural properties. EC generated fragile flocs, compared to CC, over a wider pH range, at a substantially higher growth rate, that were prone to restructuring and compaction. The results suggest that the flocculation mechanism governing EC in sweep floc conditions is of Diffusion Limited Cluster Aggregation (DCLA) nature, versus a Reaction Limited Cluster Aggregation (RLCA) type in CC. The implications of these differences are discussed.


Subject(s)
Electrocoagulation/methods , Particle Size , Alum Compounds/chemistry , Aluminum/chemistry , Electricity , Electrodes , Flocculation , Hydrogen-Ion Concentration
2.
Water Sci Technol ; 64(9): 1876-84, 2011.
Article in English | MEDLINE | ID: mdl-22020482

ABSTRACT

The main goal of this study was to examine the influence of natural organic matter (NOM) on the efficiency of H2O2/UV advanced oxidation process (AOP) as a preventive treatment for biofilm control. Pseudomonas aeruginosa PAO1 biofilm-forming bacteria were suspended in water and exposed to various AOP conditions with different NOM concentrations, and compared to natural waters. H2O2/UV prevented biofilm formation: (a) up to 24 h post treatment - when residual H2O2 was neutralized; (b) completely (days) - when residual H2O2 was maintained. At high NOM concentrations (i.e. 25 mg/L NOM or 12.5 mg/L DOC) an additive biofilm control effect was observed for the combined H2O2/UV system compared to UV irradiation alone, after short biofilm incubation times (<24 h). This effect was H2O2 concentration dependent and can be explained by the high organic content of these water samples, whereby an increase in NOM could enhance (•)OH production and promote the formation of additional reactive oxygen species. In addition, maintaining an appropriate ratio of bacterial surviving conc.: residual H2O2 conc. post-treatment could prevent bacterial regrowth and biofilm formation.


Subject(s)
Biofilms/drug effects , Organic Chemicals/pharmacology , Pseudomonas aeruginosa/physiology , Water Purification/methods , Water/pharmacology , Carbon/analysis , Hydrogen Peroxide/pharmacology , Microbial Viability/drug effects , Microbial Viability/radiation effects , Oxidation-Reduction/drug effects , Oxidation-Reduction/radiation effects , Pseudomonas aeruginosa/drug effects , Pseudomonas aeruginosa/radiation effects , Time Factors , Ultraviolet Rays
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