首页> 外文会议>Proceedings of the 11th International Conference on Fluidized Bed Technology >TWO-PHASE FLOW STRUCTURE IN A NOVEL INTERNALLY CIRCULATING FLUIDIZED BED
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TWO-PHASE FLOW STRUCTURE IN A NOVEL INTERNALLY CIRCULATING FLUIDIZED BED

机译:新型内部循环流化床中的两相流结构

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摘要

Experiments were conducted in a cold model ICFB.Transient solid holdup signals were registered and statistically analyzed.Local flow structure was discussed and evaluated.The volume fraction of the bubble/void phase increases with increasing superficial gas velocity, and decreases along axial direction, because of bubble coalescence.Standard deviation of solid holdup of the emulsion is greater in the draft tube than in the annulus, arising from stronger bubble coalescence and breakerup in the draft tube.
机译:在冷模型ICFB上进行实验,记录并统计了瞬态固体滞留信号,讨论并评估了局部流动结构,气泡/空隙相的体积分数随表观气体流速的增加而增加,并沿轴向方向减小,这是因为引流管中乳液的固体固持率的标准偏差比环空更大,这是由于引流管中更强的气泡聚结和破裂引起的。

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  • 来源
  • 会议地点 Beijing(CN)
  • 作者单位

    State Key Laboratory of Heavy Oil Processing,Faculty of Chemical Engineering,China University of Petroleum,Beijing,Changping,Beijing,P.R.China,102249;

    State Key Laboratory of Heavy Oil Processing,Faculty of Chemical Engineering,China University of Petroleum,Beijing,Changping,Beijing,P.R.China,102249;

    State Key Laboratory of Heavy Oil Processing,Faculty of Chemical Engineering,China University of Petroleum,Beijing,Changping,Beijing,P.R.China,102249;

  • 会议组织
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化工通用机械与设备;
  • 关键词

  • 入库时间 2022-08-26 14:28:58

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