Lehman S Geno, Badruzzaman Mohammad, Adham Samer, Roberts Deborah J, Clifford Dennis A
MWH Americas, Inc., 618 Michillinda Ave., Suite 200, Arcadia, CA 91007, USA.
Water Res. 2008 Feb;42(4-5):969-76. doi: 10.1016/j.watres.2007.09.011. Epub 2007 Sep 21.
Groundwater contaminated with perchlorate and nitrate was treated in a pilot plant using a commercially available ion exchange (IX) resin. Regenerant brine concentrate from the IX process, containing high perchlorate and nitrate, was treated biologically and the treated brine was reused in IX resin regeneration. The nitrate concentration of the feed water determined the exhaustion lifetime (i.e., regeneration frequency) of the resin; and the regeneration condition was determined by the perchlorate elution profile from the exhausted resin. The biological brine treatment system, using a salt-tolerant perchlorate- and nitrate-reducing culture, was housed in a sequencing batch reactor (SBR). The biological process consistently reduced perchlorate and nitrate concentrations in the spent brine to below the treatment goals of 500 microg ClO4(-)/L and 0.5mg NO3(-)-N/L determined by equilibrium multicomponent IX modeling. During 20 cycles of regeneration, the system consistently treated the drinking water to below the MCL of nitrate (10 mgNO3(-)-N/L) and the California Department of Health Services (CDHS) notification level of perchlorate (i.e., 6 microg/L). A conceptual cost analysis of the IX process estimated that perchlorate and nitrate treatment using the IX process with biological brine treatment to be approximately 20% less expensive than using the conventional IX with brine disposal.
使用市售离子交换(IX)树脂在中试装置中处理受高氯酸盐和硝酸盐污染的地下水。IX工艺产生的再生盐水浓缩液含有高浓度的高氯酸盐和硝酸盐,对其进行生物处理,处理后的盐水再用于IX树脂再生。进水的硝酸盐浓度决定了树脂的耗尽寿命(即再生频率);再生条件则由耗尽树脂的高氯酸盐洗脱曲线确定。生物盐水处理系统采用耐盐的高氯酸盐和硝酸盐还原培养物,置于序批式反应器(SBR)中。生物工艺持续将废盐水中的高氯酸盐和硝酸盐浓度降低至平衡多组分IX模型确定的500μg ClO4(-)/L和0.5mg NO3(-)-N/L的处理目标以下。在20个再生循环中,该系统持续将饮用水处理至硝酸盐最大污染物水平(MCL,10mgNO3(-)-N/L)和加利福尼亚州卫生服务部(CDHS)的高氯酸盐通报水平(即6μg/L)以下。对IX工艺的概念性成本分析估计,采用带生物盐水处理的IX工艺处理高氯酸盐和硝酸盐的成本比采用传统IX工艺并处置盐水的成本低约20%。