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使用基于氢气的膜生物膜反应器对地下水中硝酸盐和高氯酸盐生物还原动力学进行系统评估。

Systematic evaluation of nitrate and perchlorate bioreduction kinetics in groundwater using a hydrogen-based membrane biofilm reactor.

作者信息

Ziv-El Michal C, Rittmann Bruce E

机构信息

Center for Environmental Biotechnology, Biodesign Institute at Arizona State University, 1001 S. McAllister Ave., P.O. Box 875701, Tempe, AZ 85287-5801, USA.

出版信息

Water Res. 2009 Jan;43(1):173-81. doi: 10.1016/j.watres.2008.09.035. Epub 2008 Oct 11.

DOI:10.1016/j.watres.2008.09.035
PMID:18951606
Abstract

To evaluate the simultaneous reduction kinetics of the oxidized compounds, we treated nitrate-contaminated groundwater (approximately 9.4 mg-N/L) containing low concentrations of perchlorate (approximately 12.5 microg/L) and saturated with dissolved oxygen (approximately 8 mg/L) in a hydrogen-based membrane biofilm reactor (MBfR). We systematically increased the hydrogen availability and simultaneously varied the surface loading of the oxidized compounds on the biofilm in order to provide a comprehensive, quantitative data set with which to evaluate the relationship between electron donor (H(2)) availability, surface loading of the electron acceptors (oxidized compounds), and simultaneous bioreduction of the electron acceptors. Increasing the H(2) pressure delivered more H(2) gas, and the total H(2) flux increased linearly from approximately 0.04 mg/cm(2)-d for 0.5 psig (0.034 atm) to 0.13 mg/cm(2)-d for 9.5 psig (0.65 atm). This increased rate of H(2) delivery allowed for continued reduction of the acceptors as their surface loading increased. The electron acceptors had a clear hydrogen-utilization order when the availability of hydrogen was limited: oxygen, nitrate, nitrite, and then perchlorate. Spiking the influent with perchlorate or nitrate allowed us to identify the maximum surface loadings that still achieved more than 99.5% reduction of both oxidized contaminants: 0.21 mg NO(3)-N/cm(2)-d and 3.4 microg ClO(4)/cm(2)-d. Both maximum values appear to be controlled by factors other than hydrogen availability.

摘要

为了评估氧化态化合物的同步还原动力学,我们在基于氢气的膜生物膜反应器(MBfR)中处理了含有低浓度高氯酸盐(约12.5微克/升)且溶解氧饱和(约8毫克/升)的硝酸盐污染地下水(约9.4毫克氮/升)。我们系统地增加了氢气供应量,并同时改变生物膜上氧化态化合物的表面负荷,以便提供一个全面的定量数据集,用以评估电子供体(H₂)供应量、电子受体(氧化态化合物)的表面负荷以及电子受体同步生物还原之间的关系。增加氢气压力可输送更多的氢气,总氢气通量从0.5 psig(0.034 atm)时的约0.04毫克/平方厘米·天线性增加到9.5 psig(0.65 atm)时的0.13毫克/平方厘米·天。随着氧化态化合物表面负荷的增加,这种增加的氢气输送速率使得受体能够持续被还原。当氢气供应量有限时,电子受体具有明确的氢气利用顺序:氧气、硝酸盐、亚硝酸盐,然后是高氯酸盐。向进水加入高氯酸盐或硝酸盐使我们能够确定仍能实现两种氧化态污染物还原率超过99.5%的最大表面负荷:0.21毫克NO₃-N/平方厘米·天和3.4微克ClO₄/平方厘米·天。这两个最大值似乎受氢气供应量以外的因素控制。

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