Evaluation for biological reduction of nitrate and perchlorate in brine water using the hydrogen-based membrane biofilm reactor

被引:57
作者
Chung, Jinwook
Nerenberg, Robert
Rittmann, Bruce E.
机构
[1] Arizona State Univ, Biodesign Inst, Ctr Environm Biotechnol, Tempe, AZ 85287 USA
[2] Univ Notre Dame, Dept Civil Engn & Geol Sci, Notre Dame, IN 46556 USA
[3] Arizona State Univ, Ctr Environm Biotechnol, Biodesign Inst, Tempe, AZ 85287 USA
来源
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE | 2007年 / 133卷 / 02期
关键词
D O I
10.1061/(ASCE)0733-9372(2007)133:2(157)
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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 H-2-based membrane biofilm reactor (MBfR). The autotrophic biological reductions produce harmless N-2 and Cl-, making the brine safe for reuse or disposal. A very high-strength brine (similar to 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 20 g/L (similar to 2%) NaCl, while 40 g/L NaCl slowed reduction by 40% or more, confirming that the microorganisms in the MBIR were inhibited by high salt content. An increase of H-2 pressure gave higher fluxes for 20 g/L NaCl, demonstrating that H-2 availability controlled the reduction kinetics when the system was not salt-inhibited.
引用
收藏
页码:157 / 164
页数:8
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