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1.
Collection zone kinetic model for industrial flotation columns 总被引:1,自引:1,他引:1
J. Yianatos R. Bucarey J. Larenas F. Henríquez L. Torres 《Minerals Engineering》2005,18(15):1373-1377
The collection zone recovery of a flotation column was modeled using a rectangular distribution function for the kinetic rate constant and a tank in series model with different vessel sizes for the residence time distribution. It was demonstrated that an analytical expression can be obtained and that data from large industrial columns fits well, keeping the parsimony principle by using a simple and practical solution. An example for the estimation of the maximum kinetic rate constant, useful for scale-up purposes, is shown using data from industrial flotation columns. 相似文献
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This paper presents results of tests performed to investigate the effect of gas rate (1.2–2.5 cm/s), hydrophilic fines content (5–20% w/w silica) and froth depth (10–30 cm) on fines recovery in a laboratory-scale flotation column operating without wash-water addition and absence of floatable particles. A model was developed based on the entrainment coefficients presented by [Trahar, W.J., 1981. A rational interpretation of the role of particle size in flotation. International Journal of Mineral Processing 8, 289–327], which describes the mass contribution of the different size classes to the solids recovered in the concentrate. The entrainment model of [Zheng, X., Johnson, N.W., Franzidis, J.P., 2006. Modelling of entrainment in industrial flotation cells: water recovery and degree of entrainment. Minerals Engineering 19, 1191–1203] was also tested. The results show both models described well the dependence of the mass flow rate of hydrophilic solids in the concentrate. 相似文献
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Arsenic-rich, gold-bearing pyrite concentrates may be further enriched in arsenic to assist subsequent Au beneficiation. Among several amines tested in refloating a local Chalkidiki pyrite concentrate, 2-coco 2-methyl ammonium chloride proved successful by raising the grade from 9% to 22%, although total solids recovery was low. The use of a froth-stabilizing frother was also benefecial to the process. Optimum hydrohynamic conditions were: intermediate pulp flowrate, low wash water and gas flowrate; the latter abated the mixing/dispersion process in the collection zone. 相似文献
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S.R.S. Sastri P.S.R. Reddy K.K. Bhattacharyya S.G. Kumar K.S. Narasimhan 《Minerals Engineering》1988,1(4)
Tests carried out on 100mm dia × 2300mm high flotation column using coal fines from the coking coal washeries at Sudamdih, Patherdih, Kathara and Moonidih (India) have shown that the performance of the column is superior to that of the conventional cells with respect to the grade and recovery of the product. The column is found to operate efficiently both on coarse and fine fractions in the feed. The reasons for the superior performance of the flotation column have been analysed. 相似文献
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This paper presents results obtained in determining the residence time distribution (RTD) characteristics of the solid and liquid phases in a laboratory column and two industrial columns using radioactively labelled solid and liquid tracers. The dispersion model is shown to be superior to other models in describing the RTD in columns with diameter between 10cm and 150cm. Smaller diameter columns can be modelled using either the dispersion model or the tanks-in-series model and larger columns can be modelled using the latter model. Feed and gangue material produce similar tailings age distribution curves. The solid dispersion coefficient is larger than the liquid dispersion coefficient. The solid dispersion coefficient increases with increasing particle size in the laboratory column but remains constant with increasing particle size in the large columns. A modified correlation is proposed to predict the solid dispersion coefficient in large columns. 相似文献
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This paper reviews the column flotation practice in the largest Chilean copper-moly concentrators where this process unit has been increasingly chosen to replace multi stage cleaning circuits in new and existing operations. Process flowsheets incorporating columns are presented for selected concentrators. Procedures for scaling up, and process control are also illustrated. 相似文献
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将流态化机理与宽粒级煤浮选过程相结合,在一个浮选设备中实现细粒常规浮选与粗粒流态化浮选所需的不同流体力学环境,自行设计了一种新型宽粒级煤浮选机,并采用FLUENT 6.3.26软件进行数值模拟研究,从速度和湍流度两个方面对浮选机内流场进行分析。结果表明:在浮选机内增加格栅板后,可将浮选机内流场分为低速、弱湍流和高速、强湍流两个区域,从而可为粗、细颗粒浮选创造各自所需的流体力学条件;通过对叶轮圆周线速度比值与合速度比值和湍流强度比值变化规律的分析,找出浮选机模拟放大的运动相似准则。 相似文献
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This study investigates both the efficacy and selectivity temperature responsive of poly(N-isopropylacrylamide) PNIPAM as a flotation collector. The results of this study showed that charged poly(N-isopropylacrylamide) polymers selectively increased both the probability particle/bubble attachment as well as the floatability of coarse alumina and quartz particles respectively. These results provide a basis for considering PNIPAM as both an effective and selective collector in a flotation system. Coupled with previous studies that demonstrate the efficacy of PNIPAM as a flocculant in mineral suspensions, these results clearly demonstrate the potential use of PNIPAM as a dual function reagent which acts as both selective flotation collector and flocculant in the flotation of ultrafine particles. 相似文献
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Jocelyn Bouchard André Desbiens René del Villar Eduardo Nunez 《Minerals Engineering》2009,22(6):519-529
Even after having been used for several years in mineral processing plants, the full potential of the column flotation process is still not fully exploited. There is obviously more than one reason explaining this, but one important contributing factor is certainly the under usage of available control capabilities. Researchers and practitioners have been interested in column flotation simulation and control for more than two decades. This paper provides an overview of the literature focused on these specific fields of research. It also discusses some future investigative issues and how the current industry may benefit from past developments. 相似文献
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L. S. Leal Filho P. R. Seidl J. C. G. Correia L. C. K. Cerqueira 《Minerals Engineering》2000,13(14-15)
It has long been recognized that the selectivity of froth flotation processes is highly influenced by the specificity of interactions between minerals and reagents that are used to control the hydrophobic/hydrophilic character of the mineral/water interfaces. We have modelled mineral surfaces (hydroxy-apatite, calcite) and molecules of two polysaccharides (starch, ethyl-cellulose) which are candidates as depressing agents for calcite. A special parameter named “Total Fitting Number” (Ft) was developed to assess the steric compatibility between the structure of both minerals and polysaccharide species. The calculation of Ft was based on measurements of OH-OH distances that exist at reagent molecular structures versus Ca---Ca distances that exist along the most common crystallographic orientations (hkl) exhibited by mineral particles.Higher values of Ft were found for the interaction calcite/starch than calcite/ethyl-cellulose. This finding suggests that starch is a more effective depressant for calcite than ethyl-cellulose. However, low values of Ft were found for the interaction apatite/starch and apatite/ethyl-cellulose. This fact means that both substances are unlikely to act as depressants for apatite. Microflotation response of apatite and calcite with sodium oleate (pH = 10.2) in the presence of both polysaccharides corroborates the model. 相似文献
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Estimation of platinum flotation grades from froth image data 总被引:2,自引:0,他引:2
C. MaraisC. Aldrich 《Minerals Engineering》2011,24(5):433-441
Features extracted online from froth images on flotation plants are potentially useful to the development of advanced control for flotation systems, provided that these features can be related to the key indicator variables of the plant, such as valuable metal loadings and recovery. Although such relationships have been established in a number of base metal plants in industry, this is not the case in the platinum industry. In this paper, estimation of flotation grades and recoveries from froth image data is therefore considered based on laboratory and industrial plant data. It is shown that grades and recoveries can be reliably estimated from a number of different features by use of linear and nonlinear models. This includes simple colour information that on the industrial plant showed a strong correlation with grade measurement. 相似文献
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This work describes a method for supervisory control of flotation columns based on predictive trajectory generation of setpoints to be applied to the local controllers of the process. The system maximizes the profit while keeping quality constraints and engineering indices. It represents an advance over predictive supervisors using a single evaluation function or those that reduce a multi-objective problem to a single-objective one by means a weighted sum. The procedure is founded on multi-objective optimization using non-dominated genetic algorithms, and a new classification criterion of the Pareto optimal set. The system has been tested by simulation against usual perturbations affecting the flotation process and exhibits good performance, provided that the model properly represents the system operation. 相似文献
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以钱家营选煤厂浮选尾煤为对象,进行再选试验研究。对煤样进行粒度分析,发现高灰细泥含量很高,决定采用反浮选预先脱泥,并探索了药剂用量对反浮选效果的影响;脱泥后的产品进行磨矿再选,工艺流程为:"反浮选─磨矿─再选"流程,最终得到了灰分为13.96%,产率为25.96%的精煤,采用该流程处理浮选尾煤可提高选煤厂经济效益。 相似文献
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叶轮的结构型式和运行参数决定了浮选机的整体性能,结合理论分析及工程经验设计了一种功能分区的隔板叶轮。利用CFD仿真方法和试验方法对隔板叶轮的整体性能进行了测试,在仿真条件下分析了槽体内的流场结构、气液分散、功耗、循环量和吸气量等,并采用试验方法进一步对隔板叶轮的性能进行了研究,结果过表明,隔板叶轮循环量增加,吸气量略微减小,功耗略微增加,槽体下方搅拌能力增强,隔板叶轮整体性能较标准叶轮相当。 相似文献