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Radial and axial density fluctuations in a high-velocity fluidized bed.

机译:高速流化床中的径向和轴向密度波动。

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摘要

The use of gas-solid high velocity fluidized beds as catalytic chemical reactors in industrial practice is well known. A typical fast fluidized bed is operated with two distinct flow regions, a dense phase in the bottom and a dilute phase on top giving an s-shaped axial profile of the solid fraction. Recent publications show also the existence of a radial solid distribution profile with a dense wall region and a dilute core in both of the regions. Also, the occurrence of pressure waves in the lower dense region have been reported. These pressure waves, with frequencies of the order of one Hz, were interpreted as resulting from density waves. At this point in time only the first steps in describing the flow pattern for a fluidized bed operating in the high velocity fluidization regimes have been discussed.;In this work a technique is developed to directly measure instantaneous solid fractions and its radial distribution in a riser flow of air and fluid cracking catalyst. The method is based on an x-ray chordal absorptometry technique using phototransistor sensors hardwired to a computerized data acquisition system. Complementary to the x-ray measurements density fluctuations were studied using instantaneous pressure signals. Measurements were made in a high velocity fluidization unit with an inner diameter of 0.152 m and 8.4 m high. The solid used in this investigation was a Zeolite FCC catalyst, HFZ-33 (dp = 59 ;The data confirmed that the pressure readings are dependent on the spacing of the pressure probes. Decreasing the spacing of the probes leads to an increase in fluctuation amplitude and mean time average of the pressure readings, while the power spectrum shows no dependence on the spacing. To obtain reproducible data, a time average of three minutes for the pressure readings and one minute for the x-ray measurements are necessary.;Radial density profiles detected with an x-ray system in the dilute and dense phase show the existence of a core-annulus flow with a dilute core surrounded by a denser wall region. The density profiles indicate clearly that a fully developed flow pattern exists only in the dense phase.;Pressure fluctuation readings converted directly to solid fraction are larger in amplitude than the solid fraction fluctuation detected with the x-ray system. Pressure fluctuation readings are a sum of the pressure drop caused by the solid fraction in a height segment of the riser and acceleration and deceleration of the solid. The power spectra for both the pressure readings and x-ray measurements show a superimposed low frequency.
机译:在工业实践中使用气固高速流化床作为催化化学反应器是众所周知的。典型的快速流化床在两个不同的流动区域下运行,底部为浓相,顶部为稀相,给出了固体部分的S形轴向轮廓。最近的出版物还显示了径向固体分布轮廓的存在,在两个区域中都具有密集的壁区域和稀核。另外,已经报道了在较低密度区域中出现压力波。这些压力波的频率约为1 Hz,被解释为是由密度波产生的。此时,仅讨论了描述在高速流化状态下运行的流化床流型的第一步。在这项工作中,开发了一种技术,可直接测量立管中的瞬时固体成分及其径向分布空气和流体裂化催化剂的流动。该方法基于使用硬连接到计算机化数据采集系统的光电晶体管传感器的X射线弦吸收法。与X射线测量结果互补的是,使用瞬时压力信号研究了密度波动。在具有0.152m内径和8.4m高内径的高速流化单元中进行测量。本研究中使用的固体是沸石FCC催化剂HFZ-33(dp = 59;数据证实压力读数取决于压力探头的间距。减小探头间距会导致波动幅度增加)为了获得可重现的数据,压力读数的平均时间为3分钟,X射线测量的平均时间为1分钟,以获取可重现的数据。 X射线系统在稀相和稠密相中检测到的剖面表明存在一个核心环空流,稀核被较稠密的壁区域包围,密度轮廓清楚地表明只有在稠密的情况下才存在充分发展的流动模式。直接转换为固体分数的压力波动读数在幅度上大于用X射线系统检测到的固体分数波动。立管高度段中的固体分数和固体的加速和减速引起的压降的最大和。压力读数和X射线测量的功率谱都显示出叠加的低频。

著录项

  • 作者

    Feindt, Hans-Jacob.;

  • 作者单位

    City University of New York.;

  • 授予单位 City University of New York.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1990
  • 页码 114 p.
  • 总页数 114
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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