示范研究:堆浸垫排水溶液的处理:原理验证实验研究1

C. Bucknam, C. Hager
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摘要

Golder Associates进行了一项为期20周的实验研究,以确定被动处理是否能有效去除一个废弃金堆浸出垫排出的废液中的弱氰化物和NO3。选择了厌氧处理方案和三种不同的底物。三个反应器中均含有10%重量的石灰石,其中两个反应器中干草/稻草含量在80 - 90%之间,第三个反应器中干草/稻草含量为45%,马铃薯泥含量为45%。这些都是当地的农产品和副产品。由于硝酸盐- n的历史浓度范围为142至297 mg/L,因此进入反应器的流量取决于去除硝酸盐- n所需的水力停留时间,并确定为20天。3种底物对WAD氰化物和硝酸盐n的去除率分别低于0.04 mg/L和1.0 mg/L。在废水中,分析了其他可能是氰化物和硝酸盐-N降解产物的成分,仅检测到浓度为5至10 mg/L的氨-N。所有氮种中总氮的最新调节参考值设定为10 mg/L N。在此监测要求下,硝态氮和氨态氮之和将低于10 mg/L N参考值。
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DEMONSTRATION STUDY: TREATMENT OF HEAP LEACH PAD DRAIN DOWN SOLUTION: PROOF-OF-PRINCIPLE BENCH STUDY 1
A 20-week bench-scale study was conducted by Golder Associates to determine whether passive treatment could effectively remove weak and dissociable (WAD) cyanide and NO3 from the drain down solution emanating from a decommissioned gold heap leach pad. An anaerobic treatment scenario was chosen and three different substrates were chosen. Limestone at 10% by weight was in all three reactors, two of the reactors had between 80 and 90% hay/straw, and a third reactor had 45% hay/straw and 45 % potato mash. These are local agricultural products and by-products. Because the historic concentration of nitrate-N ranged from 142 to 297 mg/L, the flow rate into the reactors was based on the hydraulic retention time needed to remove nitrate-N down to 10 mg/L, and this was determined to be 20 days. All three substrates were effective at removing WAD cyanide and nitrate-N to below 0.04 mg/L and 1.0 mg/L, respectively. In the effluents, other constituents that could be the products of cyanide and nitrate-N degradation were analyzed and only ammonia- N was detected at concentrations from 5 to 10 mg/L. The most recent regulatory reference value has been set at 10 mg/L N for the total N in all nitrogen species. Under this monitoring requirement, the sum of nitrate-N and ammonia-N would be below the 10 mg/L N reference value.
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