Whereas ion exchange is an attractive technology for treating perchlorate and nitrate in drinking water, a major disadvantage is that the resin must be regenerated using a brine, producing wastes with high concentrations of nitrate, perchlorate, and salt. This study investigates the potential for simultaneous nitrate and perchlorate reductions in high-salt conditions using the H2 -based membrane biofilm reactor (MBfR). The autotrophic biological reductions produce harmless N2 and Cl− , making the brine safe for reuse or disposal. A very high-strength brine ( ∼15% salt) from a commercial ion-exchange membrane, Purolite, supported biofilm accumulation and allowed slow reduction rates for nitrate and perchlorate. Reduction rates increased significantly when the Purolite brine was diluted by 50% or more. A synthetic high-strength salt medium containing nitrate, perchlorate, or both supported more rapid reduction rates for as high as 20g∕L (∼2%) NaCl , while 40g∕L NaCl slowed reduction by 40% or more, confirming that the microorganisms in the MBfR were inhibited by high salt content. An increase of H2 pressure gave higher fluxes for 20g∕L NaCl , demonstrating that H2 availability controlled the reduction kinetics when the system was not salt-inhibited.
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Chung et al. (2007) studied this question.
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