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深錐固體通量與絮凝劑單耗和料漿濃度的數學關系

Mathematical relationship between the solid flux of deep cone thickener, flocculant unit consumption, and slurry concentration

  • 摘要: 深錐濃密機的面積或占地大小主要由其固體通量決定。通過量筒靜態沉降實驗,計算得到深錐濃密機固體通量,分析了絮凝劑單耗、料漿濃度對深錐濃密機固體通量的影響,得到了兩種因素對深錐濃密機固體通量的影響規律。結果表明,尾礦在5~30 g·t?1的絮凝劑單耗下,基本呈現二次函數關系;料漿的固相質量分數為6%~26%時,固體通量呈現先增大后減小的趨勢,與實驗所得的規律相契合。通過對絮凝劑單耗和料漿濃度耦合效應下的固體通量方程回歸分析,得到三者之間的數學關系,進而確定二者對固體通量的貢獻為:料漿濃度>絮凝劑單耗。結合絮凝劑及料漿濃度對固體通量的影響分析,總結了絮凝劑單耗和料漿濃度貢獻值不同的原因。最后,結合單因素和耦合條件下的數學方程,對深錐濃密機的設計和運行提出工程建議。在深錐濃密機運行過程中,需要優先保證料漿濃度,其次是絮凝劑單耗。

     

    Abstract: Tailings thickening is an important process of paste filling technology. At present, a deep cone thickener is often used for tailings thickening. The sedimentation rate of tailings affects the solid flux of the deep cone thickener and determines the area occupied by the deep cone thickener. At present, the addition of flocculant to tailings has become a common practice to improve the efficiency of tailings thickening. Thus, the influence of various factors on the solid flux of the deep cone thickener needs to be investigated. In this study, the solid flux of the deep cone thickener was calculated through the static sedimentation experiment of the graduated cylinder, and the influence law of the flocculant unit consumption and slurry concentration on the solid flux of the deep cone thickener was analyzed, and the influence of the two factors on the solid flux of the deep cone thickener was determined. Results showed that the tailings exhibit a quadratic function relationship when the flocculant unit consumption is 5–30 g·t?1. At 6%–26% solid mass fraction of slurry, the solid flux first increases and then decreases, which is consistent with the experiment. The regression analysis of the solid flux equation under the coupling effect of flocculant unit consumption and slurry concentration shows that the contribution of the two factors to solid flux is slurry concentration > flocculant unit consumption. Based on the analysis of the influence of flocculant unit consumption and slurry concentration on solid flux, the reasons for the different contribution values of flocculant unit consumption and slurry concentration were summarized. According to the mathematical relationship between flocculant unit consumption, slurry concentration, and solid flux obtained from the research, engineering suggestions for the design and operation of the deep cone thickener were proposed. During the operation of the deep cone thickener, the slurry concentration should be guaranteed first, followed by the flocculant unit consumption.

     

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