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Controlling the coal dust at transshipment point:A study of the foam-sol foaming device

机译:在转运点控制煤尘:泡沫溶胶发泡装置的研究

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摘要

In order to effectively control the dust at the transshipment point with foam-sol, this paper attempted to study the characteristics of dust diffusion at transshipment point and the foam-sol foaming device with diffusion outlet was also designed in this paper. To study the diffusion rules of coal dust, fluent discrete phase model was utilized in the numerical simulation, as the coal dust was thrown down at a horizontal velocity of 2.5 m/s. A foam-sol foaming device was designed, through which foaming agent could be auto-matically sucked into the Venturi by the negative pressure. The automatic controller was also equipped, which could transform the energy of the compressed air into the constant pressure difference so that the gelling agent could be qualitatively added into the gel container. The diffusion outlet that could spray out foam-sol in a continuous, conical and 3D manner was also designed. Moreover, this paper also carried out the contrast experiments on dust removal efficiency among water, aqueous foam and foam-sol. The results clearly show that the symmetrical whirlpools appeared below the inlet where the largest whirl-pool diameter was 0.52 m, and the horizontal distance from swirl range to the inlet was approximately 0.69 m. By using the self-designed foaming device, the foaming was multiplied by 30 times and the vol-ume ratio with water and foaming agent reached 95%:5%. In this context, the gas pressure was controlled at 0.3 MPa, with gas flow at 15 m3/h and water flow at 0.5 m3/h, with water pressure controlled between 0.34 and 0.36 MPa. The foam-sol has the highest dust removal efficiency than other agents.
机译:为了有效地控制泡沫-溶胶在转运点处的粉尘,尝试研究粉尘在转运点的扩散特性,并设计了带扩散出口的泡沫-溶胶发泡装置。为了研究煤尘的扩散规律,在数值模拟中使用了流态离散相模型,因为煤尘以2.5 m / s的水平速度被抛落。设计了一种泡沫溶胶发泡装置,通过该装置可以将发泡剂在负压下自动吸入文丘里管。还配备了自动控制器,该控制器可以将压缩空气的能量转换为恒定压力差,从而可以将胶凝剂定性地添加到凝胶容器中。还设计了可以连续,锥形和3D方式喷出泡沫溶胶的扩散出口。此外,本文还对水,泡沫水和泡沫溶胶之间的除尘效率进行了对比实验。结果清楚地表明,对称涡流出现在最大涡流直径为0.52 m的入口下方,并且从旋流范围到入口的水平距离约为0.69 m。通过使用自行设计的发泡装置,发泡倍增30倍,与水和发泡剂的体积比达到95%∶5%。在此情况下,将气压控制在0.3 MPa,气流控制在15 m3 / h,水流控制在0.5 m3 / h,水压控制在0.34和0.36 MPa之间。泡沫溶胶的除尘效率最高。

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  • 来源
    《矿业科学技术(英文版)》 |2014年第5期|625-630|共6页
  • 作者单位

    School of Environmental Science and Safety Engineering, Tianjin University of Technology, Tianjin 300384, China;

    School of Environmental Science and Safety Engineering, Tianjin University of Technology, Tianjin 300384, China;

    Tianjin Key Laboratory for Control Theory&Application in Complicated Systems, Tianjin University of Technology, Tianjin 300384, China;

    School of Environmental Science and Safety Engineering, Tianjin University of Technology, Tianjin 300384, China;

  • 收录信息 中国科技论文与引文数据库(CSTPCD);
  • 原文格式 PDF
  • 正文语种 eng
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