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Slurry bubble column hydrodynamics.

机译:浆料鼓泡塔流体力学。

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摘要

Slurry bubble column reactors are presently used for a wide range of reactions in both chemical and biochemical industry. The successful design and scale up of slurry bubble column reactors require a complete understanding of multiphase fluid dynamics, i.e. phase mixing, heat and mass transport characteristics.; The primary objective of this thesis is to improve presently limited understanding of the gas-liquid-solid slurry bubble column hydrodynamics. The effect of superficial gas velocity (8 to 45 cm/s), pressure (0.1 to 1.0 MPa) and solids loading (20 and 35 wt.%) on the time-averaged solids velocity and turbulent parameter profiles has been studied using Computer Automated Radioactive Particle Tracking (CARPT). To accomplish this, CARPT technique has been significantly improved for the measurements in highly attenuating systems, such as high pressure, high solids loading stainless steel slurry bubble column. At a similar set of operational conditions time-averaged gas and solids holdup profiles have been evaluated using the developed Computed Tomography (CT)/Overall gas holdup procedure. This procedure is based on the combination of the CT scans and the overall gas holdup measurements. The procedure assumes constant solids loading in the radial direction and axially invariant cross-sectionally averaged gas holdup.; The obtained experimental holdup, velocity and turbulent parameters data are correlated and compared with the existing low superficial gas velocities and atmospheric pressure CARPT/CT gas-liquid and gas-liquid-solid slurry data. The obtained solids axial velocity radial profiles are compared with the predictions of the one dimensional (1-D) liquid/slurry recirculation phenomenological model. The obtained solids loading axial profiles are compared with the predictions of the Sedimentation and Dispersion Model (SDM). The overall gas holdup values, gas holdup radial profiles, solids loading axial profiles, solids axial velocity radial profiles and solids shear stress radial profiles are correlated using several widely used empirical correlations that are modified and improved to better represent present data.
机译:浆态鼓泡塔反应器目前在化学和生化工业中用于广泛的反应。浆液鼓泡塔反应器的成功设计和规模化需要对多相流体动力学,即相混合,传热和传质特性有完整的了解。本文的主要目的是改善目前对气液固浆鼓泡塔流体动力学的有限理解。使用计算机自动技术研究了表观气体速度(8至45 cm / s),压力(0.1至1.0 MPa)和固体载量(20和35 wt。%)对时间平均固体速度和湍流参数分布的影响放射性粒子跟踪(CARPT)。为此,在高度衰减系统(例如高压,高固体含量的不锈钢浆料鼓泡塔)中进行测量时,CARPT技术已得到显着改进。在一组类似的操作条件下,已使用开发的计算机断层扫描(CT)/总体气体滞留程序评估了平均时间的气体和固体滞留曲线。此过程基于CT扫描和整体气体滞留量测量值的组合。该程序假设固体在径向上的载荷恒定,并且轴向上的横截面平均持气量不变。将获得的实验滞留量,速度和湍流参数数据进行关联,并与现有的低表观气体速度和大气压CARPT / CT气液和气液固浆数据进行比较。将获得的固体轴向速度径向轮廓与一维(1-D)液体/淤浆再循环现象学模型的预测值进行比较。将获得的固体载荷轴向轮廓与沉降和弥散模型(SDM)的预测值进行比较。使用几个广泛使用的经验相关性对总气体含气量值,气体含气径向轮廓,固体载荷轴向轮廓,固体轴向速度径向轮廓和固体剪切应力径向轮廓进行关联,这些经验相关性经过修改和改进以更好地表示当前数据。

著录项

  • 作者

    Rados, Novica.;

  • 作者单位

    Washington University.;

  • 授予单位 Washington University.;
  • 学科 Engineering Chemical.; Physics Fluid and Plasma.
  • 学位 D.Sc.
  • 年度 2003
  • 页码 p.2792
  • 总页数 260
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化工过程(物理过程及物理化学过程);
  • 关键词

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