Dareh Alou浓密尾砂管理方案:设计注意事项

A. Roshdieh, K. Seddon, M. Mohebbi, K. Shakeri, M. Nosrati
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摘要

本文介绍了伊朗Dareh Alou露天铜矿加厚尾砂储存设施(TSF)设计的一个案例研究。Dareh Alou铜矿是伊朗国家铜业公司(NICICO)拥有的一座新铜矿。它位于伊朗伊斯兰共和国的克尔曼省。名义产量为700万吨/年,矿山寿命为25年。为容纳总计175公吨的尾矿进行了规划。Dareh Alou矿区位于山谷的斜坡上,周围环绕着小山,地势陡峭。由于这是一个绿地项目,选矿厂的地点是与尾矿沉积方案研究一起选定的。考察了五个具有不同矿石运输选择的选矿厂地点,并对尾矿和水管理进行了研究。研究结果表明,最佳选矿厂的位置是在距离首选TSF位置约2.5公里的RL 3050米处。评估了各种尾矿和水管理方案,包括高倍率、高密度/高压缩和膏体增稠剂。研究了这些脱水选择以及各种TSF和增稠器位置的组合。选择研究的结果表明,如果补充水的价格不包括在分析中,首选的选择是使用高速率增稠剂。然而,在以1美元/立方米的速率加入补充水之后,首选的选择是使用高密度/高压缩稠化剂。在这种情况下,由于选矿厂与尾矿堆之间的距离较远,因此将未浓缩的尾矿输送到位于尾矿堆附近的浓缩厂是最有效的选择。此外,尽管需要相对较大的堤防来封闭山谷场地,但将尾矿加厚将有助于降低堤防建设成本。
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Dareh Alou thickened tailings management scheme: design considerations
This paper presents a case study on the design of a thickened tailings storage facility (TSF) for a proposed open pit copper mine at Dareh Alou, Iran. Dareh Alou mine is a new copper mine owned by National Iranian Copper Company (NICICO). It is located in the Kerman Province of the Islamic Republic of Iran. The nominal production rate is 7 Mtpa for a life-of-mine (LOM) of 25 years. Planning was undertaken for the accommodation of a total of 175 Mt of tailings. The Dareh Alou mine site is located on a sloping side of a valley that is surrounded by hills, grading up to steep mountainous terrain. Since this is a greenfield project the location of the concentrator was selected in conjunction with the tailings deposition options study. Five concentrator locations with various ore transportation options have been investigated together with the tailings and water management study. The result of the study indicated that the best concentrator plant location was at RL 3050 m at approximately 2.5 km from the preferred TSF location. Various tailings and water management options were evaluated, including high rate, high density/high compression, and paste thickeners. These dewatering options were studied alongside the combinations of various TSF and thickener locations. The outcome of the options study indicates that if the price of make-up water is not included in the analyses, the preferred option is utilisation of high rate thickeners. However, after inclusion of make-up water at a rate of USD 1/m3, the preferred option would be the utilisation of high density/high compression thickeners. In this case, the distance between the concentrator and the TSF is such that transportation of un-thickened tailings to thickeners located adjacent to the TSF is the most efficient option. Also, thickening the tailings will provide benefits in reducing the embankment construction cost even though relatively large embankments will be required to close off the valley site.
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