首页> 外文会议>International Seminar on Paste and Thickened Tailings >Recycling fine slurry - an alternative to paste for coarse rejects co-disposal in Queensland coal mines
【24h】

Recycling fine slurry - an alternative to paste for coarse rejects co-disposal in Queensland coal mines

机译:回收精细浆料 - 施用粗拒绝在昆士兰州煤矿共同处理的替代品

获取原文

摘要

Conventional co-disposal of coarse rejects (minus 50 mm) and fine thickener underflow tailings (minus 2 mm) is practised at a number of Queensland coal mines. The two streams are combined and pumped together to disposal. However, with the ratio of coarse rejects to tailings typically being about 70:30 on a dry mass basis, it is necessary to add large quantities of water to reduce the volume concentration of coarse rejects to an acceptable pumpable level. At the disposal site, the low concentration fines wash through the coarse rejects, forming a pond at the toe of the deposit. Water needs to be recovered from the pond and pumped back to the plant, and some water is lost through evaporation. The deposit also requires significant management with earthmoving equipment.An alternative co-disposal system is described, in which no dilution water is required. By recycling some of the minus 2 mm thickener underflow in a recycle pipeline, the required reduction in volume concentration of rejects in the mixture is achieved without water dilution. With a thickener underflow concentration of 50% by weight (w/w), the total mixture concentration discharged to disposal is up to 75% w/w, and the discharged mixture is essentially homogeneous with minimal separation of fines. The emplacement can take the form of a cone-shaped deposit, thereby greatly reducing the earthworks required. The net effect is that total costs are about half of that required for the current co-disposal systems.The 75% w/w concentration achieved by recycling fines is similar to the concentration likely to be delivered by proposed laminar flow paste pipeline systems, and is achieved with more reliable turbulent flow operation, avoiding the uncertainties associated with laminar flow.
机译:在许多昆士兰煤矿上实施常规腐烂(减去50 mm)和细增稠剂下尾(减去2mm)的细增稠剂尾部(减去2mm)。两条溪流组合并泵组一起处理。然而,随着粗拒绝与尾矿的比率通常在干块的基础上为约70:30,需要增加大量的水以将粗糙的抑制的体积浓度降低到可接受的泵送水平。在处理现场,低浓度细粉通过粗拒污染,在矿床的脚趾上形成池塘。需要从池塘中恢复水并抽回工厂,通过蒸发损失一些水。矿床还需要与地耕设备进行重大管理。描述了替代的共处理系统,其中不需要稀释水。通过回收循环管道中的一些减去欠溢的减去2mm的溢出器,在没有水稀释的情况下达到混合物中废物体积浓度的所需浓度降低。具有50重量%(w / w)的增稠剂溢出浓度(w / w),排放到处理的总混合浓度高达75%w / w,并且排出的混合物基本上具有最小的细粒分离。施加可以采用锥形沉积物的形式,从而大大减少了所需的土方工程。净效应是总成本约为当前共处理系统所需的一半。通过回收罚款实现的75%W / W浓度类似于可能通过提出的层流膏管道系统提供的浓度,以及通过更可靠的湍流操作实现,避免与层流相关的不确定性。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号