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THE EFFECT OF REPULPING ON THE SX7 SPIRAL

机译:在SX7螺旋上擦除的效果

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Spirals concentrators are widely used for beneficiation of fine coal typically the -1mm size fraction. The repulper and the splitter on the SX7 spiral play a vital role in determining the final product ash. The splitter separates the material after the 3rd turn into two streams; high ash and low ash streams. The high ash stream is channeled into the center column while the low ash is directed into the repulper. The material in the center column is collected at the end of the spiral trough as a reject fraction. The low ash fraction on the other hand is mixed again in the repulper and given a second chance for further rejection of ash. The aim of the study was to evaluate the metallurgical performance of the new SX7 spiral with a drop-in repulper design. Three models of the SX7 spirals were tested and compared, the SX7 without a repulper, the SX7 with the old repulper design and the new SX7 with a drop-in repulper design. The spiral without repulper was tested to provide a benchmark against which the spirals with the different repulper designs were compared; all spirals were tested at 25%, 30% and 35% solids concentration. The solids feed rate was kept constant around 3tph. The product samples were analyzed for ash and calorific value (CV). The findings consistently show that there are no differences in ash and CV contents achieved in the concentrate fractions on both spirals at various solids concentrations. The mass yield on the old spiral is however higher than on the new spiral, at the same splitter setting for all the tests at various solids concentrations. This could possibly be explained by the fact that on the old SX7 spiral, a gap is created between the bottom of the splitter and the trough floor and allows the material to seep through to the repulper. This furthermore suggests that there is room on the new spiral for the splitter position to be slightly closed to allow more material to go through the repulper section to obtain more mass yield without increasing the concentrate ash. The results show that the modifications done on the new SX7 spiral have not negatively affected the metallurgical performance of the spiral. The new SX7 spiral with a drop in repulper allows for replacement of the repulper and the lid when worn out. The spiral has a fixed hollow area where the repulper fits; this is expected to eliminate the inconsistencies as a result of variability in assembly. The new lid does not compress the edge rubber as before, and as a result spillages are eliminated. On the new spiral, the material bypass has been eliminated, the shape of the splitter follows the trough profile, the floor of the spiral where the splitter sits has been made such to ensure that the splitter sits flat on the spiral trough and does not create a gap. The splitter is also longer than on the old spiral, this is expected to provide flexibility to open the splitter wider to only direct a narrow stream to the repulper if a lower ash product is required.
机译:螺旋集中器被广泛地用于粉煤通常是-1mm大小部分的选矿。碎浆机并在SX7分离器螺旋在决定最终产品的灰分起着至关重要的作用。分路器之后的第三转弯成两个流的材料分离;高灰,低灰流。而低灰分被引导到再浆化槽的高灰分流被引导到所述中心柱。在中央柱中的材料在螺旋槽的端部被收集作为废弃部分。在另一方面低灰分馏分在再浆化槽再次混合,并给出了进一步抑制灰的第二次机会。这项研究的目的是评估与一个下拉碎浆机设计的新SX7螺旋的冶金性能。该SX7螺旋的三种模式进行了测试和比较,SX7没有碎浆机,与旧的碎浆机的设计和带有一个下拉式碎浆机设计的新SX7的SX7。没有再浆螺旋进行测试,以便提供针对其与再浆化槽不同设计螺旋进行比较的基准;所有螺旋在25%,30%和35%的固体浓度下测试。固体进给速度保持周围3tph不变。该产品样本进行了分析灰分和热值(CV)。研究结果一致表明有在不同固体浓度二者螺旋在浓缩物的级分来实现灰和CV含量没有差异。在老螺旋质量产率然而比对新高的螺旋,在相同的分离器设置在不同的固体浓度的所有测试。这可能会因该对旧SX7螺旋,被分离器的底部与所述槽地板之间产生间隙,并允许该材料渗漏通过对再浆化槽的事实来解释。此外,这表明,有空间上的分离器的位置的新的螺旋被稍微关闭,以允许更多的材料要经过碎浆机段以获得更多的质量产率而不增加浓缩物灰。结果表明,在新的SX7螺旋所做的修改还没有螺旋的冶金性能产生负面影响。在碎浆机中下降的新SX7螺旋允许更换碎浆机的,当磨损盖子。所述螺旋具有固定中空其中区域中的再浆化槽配合;这是预期的,以消除不一致性变异性组件的结果。新的盖不压缩,端部橡胶和以前一样,并且作为结果溢出物被消除。在新的螺旋,所述材料旁路已被消除,分离器的形状遵循槽轮廓,螺旋的地板,其中分离器坐在已经做出这样,确保了分离器平放在螺旋槽,并且不产生一个沟。这个分离器也比对旧螺旋更长的时间,这是预期的,以提供灵活性以打开分配器更宽以仅当需要较低的灰产品引导窄流至再浆化槽。

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