4.8 Article

Predicting the Contribution of Chloramines to Contaminant Decay during Ultraviolet/Hydrogen Peroxide Advanced Oxidation Process Treatment for Potable Reuse

Journal

ENVIRONMENTAL SCIENCE & TECHNOLOGY
Volume 53, Issue 8, Pages 4416-4425

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acs.est.8b06894

Keywords

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Funding

  1. Water Research Foundation [Reuse-16-01]
  2. National Science Foundation Engineering Research Center for Re-Inventing the Nation's Urban Water Infrastructure (ReNUWIt) [EEC-1028968]

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Chloramines applied to control membrane biofouling in potable reuse trains pass through reverse osmosis membranes, such that downstream ultraviolet (UV)/H2O2 advanced oxidation processes (AOPs) are de facto UV/H2O2-chloramine AOPs. Current models for UV/chloramine AOPs, which use inaccurate chloramine quantum yields and ignore the fate of (NH2)-N-center dot, are unable to simultaneously predict the loss of chloramines and contaminants, such as 1,4-dioxane. This study determined quantum yields for NH2Cl (0.35) and NHCl2 (0.75). Incorporating these quantum yields and the formation from (NH2)-N-center dot of the radical scavengers, (NO)-N-center dot and NO2-, was important for simultaneously modeling the loss of chloramines, H2O2, and 1,4-dioxane in the UV/H2O2-chloramine AOP. Although the level of radical production was higher for the UV/H2O2-chloramine AOP than for the UV/H2O2 AOP, the UV/H2O2 AOP was at least 2-fold more efficient with respect to 1,4-dioxane degradation, because chloramines efficiently scavenged radicals. At low chloramine concentrations, the UV/chloramine AOP efficiency increased with an increase in chloramine concentration, as the level of radical production increased relative to that of radical scavenging by the dissolved organic carbon in RO permeate. However, the efficiency leveled out at higher chloramine concentrations as radical scavenging by chloramines offset the increased level of radical production. The level of 1,4-dioxane degradation was similar to 30-50% lower for the UV/chloramine AOP than for the UV/H2O2-chloramine AOP when the concentration of residual chloramines in RO permeate was similar to 50 mu M (3.3 mg/L as Cl-2). Initial cost estimates indicate that the UV/chloramine AOP using the residual chloramines in RO permeate could be a cost-effective alternative to the current UV/H2O2-chloramine AOP in some cases, because the savings in reagent costs offset the similar to 30-50% reduction in 1,4-dioxane degradation efficiency.

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