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A concurrent flotation column for fly ash cleaning and materials separation: Its design and separation system development.

机译:用于粉煤灰清洁和物料分离的同时浮选柱:其设计和分离系统的开发。

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摘要

In order to widely reuse fly ash, which was previously landfilled, the unburned carbons must be removed to below 1% in cleaned fly ash. This research is aimed at developing a highly efficiency and effective flotation process and equipment for fly ash cleaning and materials' separation.;The froth flotation process is an approximate first-order reaction. Hence, a concurrent flotation column, which can closely simulate a plug flow reactor, has a high potential to resolve the problems, such as high energy consumption and low separation efficiency, existing in commercial flotation machines. Based on the above considerations, a concurrent flotation column has been developed by combining a static mixer and froth separator.;Experimental results have shown that the carbon removal under a concurrent flotation column with one static mixer is 22% below that of the Denver Cell. Mechanism analysis showed that froth rupture might occur along a static mixer. The froth formation and breakage in a static mixer are a reversible process. Therefore, a perfect carbon removal could not be achieved using only one static mixer.;Using dual static mixers, the carbon removal was elevated slightly higher than that of the Denver Cell. The concurrent flotation column shows an obviously higher throughput. Moreover, the energy consumption of a concurrent flotation column is only 20% of the Denver Cell.;The size of air bubbles produced from a static mixer is significantly correlated to the surface tension, air flowrate and channel number of packings. Bubble size increases with surface tension, but decreases with the increase of air flowrate and channel number.;In conclusion, the concurrent flotation column has proved to be a highly effective and efficient flotation device. Its extremely low energy cost and high unit throughput would significantly reduce the operation cost of fly ash cleaning, and potentially extend its applications in other industries.
机译:为了广泛地利用以前被填埋的粉煤灰,必须将清洁的粉煤灰中未燃烧的碳清除至1%以下。这项研究旨在开发一种高效,有效的浮选工艺和设备,用于粉煤灰的清洁和物料的分离。泡沫浮选工艺是一种近似的一级反应。因此,可以紧密模拟活塞流反应器的并发浮选塔具有解决商业浮选机中存在的诸如高能耗和低分离效率的问题的高潜力。基于上述考虑,通过组合静态混合器和泡沫分离器,开发了同时浮选塔。实验结果表明,采用一台静态混合器在同时浮选塔下的除碳量比丹佛电解池低22%。机理分析表明,泡沫破裂可能会在静态混合器上发生。静态混合器中的泡沫形成和破裂是可逆的过程。因此,仅使用一个静态混合器就无法达到理想的除碳效果。使用双静态混合器,除碳的效率略高于丹佛电解池。同时浮选柱显示出明显更高的产量。此外,并发浮选柱的能耗仅为丹佛电解池的20%。静态混合器产生的气泡大小与表面张力,空气流速和填料通道数显着相关。气泡的大小随表面张力的增加而增加,但随空气流量和通道数的增加而减小。总之,同时浮选塔被证明是一种高效的浮选装置。其极低的能源成本和高单位吞吐量将大大降低粉煤灰清洁的运营成本,并有可能将其扩展到其他行业。

著录项

  • 作者

    Xiao, Chuanfu.;

  • 作者单位

    Michigan Technological University.;

  • 授予单位 Michigan Technological University.;
  • 学科 Engineering Mechanical.;Engineering Metallurgy.;Engineering Environmental.
  • 学位 Ph.D.
  • 年度 1997
  • 页码 230 p.
  • 总页数 230
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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