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METHOD FOR OBTAINING ORE/MINERAL CONCENTRATES FROM RAW ORES/RAW MATERIALS AND A JIG THEREFOR

机译:从矿石/原材料中获取矿石/矿物精矿的方法及其夹具

摘要

In jigging for purposes of gravity separation of material to be concentrated the material is sorted into a heavy fraction which is withdrawn through a screen (2) and a light fraction withdrawn above the screen (2), by periodically passing flows from the bottom to the top through the feed material. If the material is predominantly of finer character, there will be a ragging (3) on the screen (2) composed of particles which are larger and usually also specifically heavier than those of the feed material. In this manner, however, the separation of feed material will be unsatisfactory in the fine particle size range having upper particle size limits between 300 mu m and 1 mm, particularly so if the particle size ratio of the material is rather broad. To obtain high-grade concentrates, and high yields at the same time, also in the fine particle size range mentioned and in the finest particle size range below the same, therefore, it is provided that, below the feed bed (5) a filter layer (4) is introduced which consists of particles having a density approximately the same as that of the heavy fraction and a size which is within the limits of from 1.2 to 2.5 times the upper particles size limit of the feed material, the height of the filter layer corresponding to at least twice the mean particle size of the filter layer particles, that, for jigging, the feed bed (5) first is stratified such that the finer particles of the specifically lighter material mainly are moved into the upper part of the feed bed (5), and that, during jigging, the periodic inflowing is effected or adjusted in frequency such that the filter layer will adopt a porosity of between 60% and 70% by the upward stroke and the stroke amplitude will range between 50% and 200% of the filter layer height. A jig for carrying out the method is disclosed as well.
机译:出于重力分离的目的,通过周期性地将水从底部流到筛子,将物料分为重馏分并通过筛网(2)抽出,轻馏分从筛网(2)上方抽出。穿过饲料原料。如果物料主要是较细的物料,则在筛网(2)上会出现碎屑(3),该碎屑(3)由比进料物料更大且通常也比物料重的颗粒组成。然而,以这种方式,进料的分离在具有300μm和1mm之间的上限的粒径上限的细粒径范围内将是不令人满意的,特别是如果原料的粒径比相当宽的话。为了同时获得高品质的浓缩物和高收率,同样在所述的细粒度范围内和在其以下的最细粒度范围内,因此提供在进料床(5)下方的过滤器引入层(4),该层由密度与重质馏分的密度大致相同并且尺寸在进料的最大颗粒尺寸上限1.2-2.5倍的范围内的颗粒组成,至少对应于滤料层颗粒平均粒径至少两倍的滤料层,该层为了进行摇动,首先将进料床(5)分层,使特定较轻材料的较细颗粒主要移入滤料层的上部。进料床(5),并且在跳动过程中会进行周期性的流入或调整频率,以使过滤层的向上冲程的孔隙率在60%到70%之间,冲程幅度在50%的范围内和过滤层高度的200%。还公开了用于执行该方法的夹具。

著录项

  • 公开/公告号IN165795B

    专利类型

  • 公开/公告日1990-01-13

    原文格式PDF

  • 申请/专利权人 SCHONERT KLAUS;

    申请/专利号IN408CA1986

  • 发明设计人 SCHONERT KLAUS;GERSTENBERG ROLF;

    申请日1986-06-02

  • 分类号B03B5/00;

  • 国家 IN

  • 入库时间 2022-08-22 06:18:34

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