Wani Altaf H, O'Neal Brenda R, Gilbert David M, Gent David B, Davis Jeffrey L
Applied Research Associates, Inc., 119 Monument Place, Vicksburg, MS 39180, USA.
Chemosphere. 2006 Feb;62(5):689-98. doi: 10.1016/j.chemosphere.2005.06.012. Epub 2005 Aug 2.
Electrolytic reactive barriers (e(-) barriers) consist of closely spaced permeable electrodes installed across a groundwater contaminant plume in a permeable reactive barrier format. Application of sufficient potential to the electrodes results in sequential oxidation and reduction of the target contaminant. The objective of this study was to quantify the mass distribution of compounds produced during sequential electrolytic oxidation and reduction of ordinance related compounds (ORCs) in a laboratory analog to an e(-) barrier. In this study, a series of column tests were conducted using RDX (hexahydro-1,3,5-trinitro-1,3,5-triazine) and TNT (2,4,6-trinitrotoluene) as representative ORCs. The experimental setup consisted of a plexiglass column packed with quartz-feldspar sand to simulate aquifer conditions. A single set of porous electrodes consisting of expanded titanium-mixed metal oxide mesh was placed at the midpoint of the sand column as a one-dimensional analog to an e(-) barrier. Constant current of 20mA (variable voltage) was applied to the electrode set. Initial studies involved quantification of reaction products using unlabeled RDX and TNT. Approximately 70% of the influent concentration was transformed, in one pass, through sequential oxidation-reduction for both contaminants. Following the unlabeled studies, (14)C labeled RDX and TNT were introduced to determine the mass balance. An activity balance of up to 96% was achieved for both (14)C-RDX and (14)C-TNT. For both contaminants, approximately 21% of the influent activity was mineralized to (14)CO(2). The proportion of the initial activity in the dissolved fraction was different for the two test contaminants. Approximately 30% of the initial (14)C-RDX was recovered as unreacted in the dissolved phase. The balance of the (14)C-RDX was recovered as non-volatile, non-nitroso transformation products. None of the (14)C-RDX was sorbed to the column sand packing. For (14)C-TNT approximately 51% of the initial activity was recovered in the dissolved phase, the majority was unreacted TNT. The balance of the (14)C-TNT was either sorbed to the sand packing (approximately 24%) or dissolved/mineralized as unidentified ring cleavage products ( approximately 4%).
电解反应屏障(电子屏障)由以渗透反应屏障形式横跨地下水污染物羽流安装的紧密间隔的可渗透电极组成。向电极施加足够的电势会导致目标污染物依次发生氧化和还原。本研究的目的是在一个模拟电子屏障的实验室环境中,量化在依次进行电解氧化和还原与爆炸物相关化合物(ORC)过程中产生的化合物的质量分布。在本研究中,使用黑索今(六氢-1,3,5-三硝基-1,3,5-三嗪)和三硝基甲苯(2,4,6-三硝基甲苯)作为代表性的ORC进行了一系列柱试验。实验装置由一个填充石英长石砂以模拟含水层条件的有机玻璃柱组成。一组由膨胀钛混合金属氧化物网组成的多孔电极放置在砂柱的中点,作为电子屏障的一维模拟。向电极组施加20mA的恒定电流(可变电压)。初步研究涉及使用未标记的黑索今和三硝基甲苯对反应产物进行定量。两种污染物在一次通过时,约70%的进水浓度通过依次氧化还原被转化。在未标记研究之后,引入了碳-14标记的黑索今和三硝基甲苯以确定质量平衡。碳-14标记的黑索今和碳-14标记的三硝基甲苯均实现了高达96%的活性平衡。对于两种污染物,约21%的进水活性被矿化生成二氧化碳。两种测试污染物在溶解部分的初始活性比例不同。约30%的初始碳-14标记的黑索今在溶解相中以未反应形式回收。碳-14标记的黑索今的其余部分以非挥发性、非亚硝基转化产物的形式回收。没有碳-14标记的黑索今吸附到柱砂填料上。对于碳-14标记的三硝基甲苯,约51%的初始活性在溶解相中回收,大部分是未反应的三硝基甲苯。碳-14标记的三硝基甲苯的其余部分要么吸附到砂填料上(约24%),要么作为未鉴定的开环产物溶解/矿化(约4%)。