Mixing requirement for ultra paste tailings

A. Roshdieh, S. Javadi, M. Williams, E. Karamad
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Abstract

A controlling variable for a thickened tailings scheme design is the beach slope that will be formed by the tailings as they deposit. The slope will be mainly related to the discharge flow rate and the slurry rheology. The latter will, in turn, be dependent on the solids concentration of the thickener underflow. A higher solids concentration can be achieved by combining thickening and filtration. The objective is to still maintain a slurry that is pumpable and self-distributing at the tailings storage facility (TSF), rather than having to rely on trucks or on conveyors and stacking systems to manage a ‘cake’, but one that will deposit at a steeper beach slope than can be achieved by thickening alone. The use of ultra paste has the potential to broaden the range of topographic conditions that will suit thickened tailings discharge. The ultra paste thickened option is when a portion of the tailings is separated and dewatered in a more advanced dewatering unit (in this case filter presses). The filtered cake will then be re-mixed with the paste thickener underflow stream. This paper presents a case study for a large copper mine in which underflow from a series of paste thickeners with a nominal tonnage of 3,660 tph at 59% solids concentration would be mixed with 1,363 tph of filter cake at 80% solids concentration. The combined tailings (ultra paste) would be discharged equally into two open channels (flumes) at the combined solids concentration of 63.5%. The ultimate goal of adopting an ‘ultra paste’ scheme is to produce homogenous consistency tailings, hence proper mixing of the paste and filter cake has to occur. In this study based on a series of tests, the mixing requirement has been assessed. The study also covers a conceptual investigation of natural turbulent mixing (NTM) of the filtered tailings with paste thickened tailings and issues associated with the deposition of the combined tailings, the ultra paste, into the existing TSF. In the conclusion, the study indicates that NTM can possibly occur only for the case in which the total tailings are discharged into one channel, which is not practical due to limitations with regards to tailings management. Hence, mechanical mixing has been recommended in this case.
超膏体尾矿混合要求
浓密尾砂方案设计的一个控制变量是尾砂在沉积过程中形成的滩坡。边坡主要与排料流量和料浆流变有关。后者反过来又取决于增稠器底流的固体浓度。通过稠化和过滤相结合可以获得更高的固体浓度。目标是在尾矿储存设施(TSF)中保持可泵送和自分布的泥浆,而不是依靠卡车或输送机和堆叠系统来管理“蛋糕”,但它将沉积在更陡峭的海滩斜坡上,而不是单独增稠。使用超级膏体有可能扩大适合浓缩尾矿排放的地形条件范围。超膏体浓缩选择是当一部分尾矿被分离并在更先进的脱水装置中脱水(在这种情况下是压滤机)。过滤后的饼将与膏体增稠机底流重新混合。本文介绍了一个大型铜矿的案例研究,其中标称吨位为3660吨/小时、固体浓度为59%的一系列膏体增稠机的底液将与固体浓度为80%的1363吨/小时滤饼混合。组合尾砂(超膏体)在组合固体浓度为63.5%时均匀排入两个明渠(水槽)。采用“超级膏体”方案的最终目标是产生均匀稠度的尾矿,因此膏体和滤饼必须进行适当的混合。本研究在一系列试验的基础上,对混合要求进行了评估。该研究还涵盖了对过滤后的尾矿与膏体浓缩尾矿的自然湍流混合(NTM)的概念调查,以及与组合尾矿(超膏体)沉积到现有TSF中的相关问题。在结论中,研究表明,NTM只有在全尾砂排入一个通道的情况下才有可能发生,由于尾砂管理的限制,这种情况是不现实的。因此,在这种情况下,建议采用机械搅拌。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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