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Granular flow, segregation and agglomeration in bladed mixers.

机译:叶片混合器中的颗粒流,分离和附聚。

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摘要

A large number of industrial processes involve the transport, mixing and storage of particulate systems. While prevalent in industry, particulate processes are commonly plagued by problems due to the complex rheology of these systems. In this work, the behavior of granular materials in a bladed mixer, an industrially relevant geometry, was investigated using computational and experimental techniques. Experimental flows were characterized via Particle Image Velocimetry and image analysis. Discrete element simulations were carried out to examine the effect of a wide range of system parameters.;Particulate flows in bladed mixers were found to be periodic with complex flow patterns developing throughout the particle bed. Cohesionless flows were initially studied. For monodisperse flows, two distinct flow regimes were observed: a quasi-static regime where blade speed provides the time scale for momentum transfer and an intermediate regime where stresses scale linearly with blade speed. Particle and wall roughness were found to significantly affect bladed mixer flows. Systems with higher roughness are characterized by enhanced particle motion and mixing. Simple scaling relationships were observed for monodisperse flows in the quasi-static regime. Particle velocities and diffusivities were found to scale linearly with mixer size and blade speed, while stresses scaled linearly with particle bed weight. In polydisperse flows, size segregation was found to occur due to sieving. However, it was found that the extent of segregation can be reduced by introducing intermediate particle sizes in between the smallest and largest particles.;Finally, wet particle flows were examined. At low moisture contents, enhanced particle velocities and mixing kinetics were observed in comparison to dry flows. However, at higher moisture contents, particle velocities and mixing rates were observed to decrease. Wet particle flows were characterized by the formation of particle agglomerates. Agglomerate formation led to an increase in particle bed roughness which significantly influenced macroscopic and microscopic flow properties.;These findings contribute to the understanding of granular behavior in complex systems. Improved understanding of granular flows will enable the development of first-principles based models which can assist in the design and scale-up of bladed mixer operations and the identification of critical processes parameters.
机译:大量工业过程涉及颗粒系统的运输,混合和储存。尽管在工业中很普遍,但是由于这些系统的复杂流变性,微粒工艺通常会遇到问题。在这项工作中,使用计算和实验技术研究了颗粒状物料在叶片搅拌机中的行为,这是一种与工业相关的几何形状。通过粒子图像测速和图像分析来表征实验流程。进行了离散元模拟,以检验各种系统参数的影响。;发现叶片式混合器中的颗粒流是周期性的,并且整个颗粒床中形成复杂的流型。最初研究了无内聚流。对于单分散流,观察到两种截然不同的流态:准静态态,叶片速度为动量传递提供时间尺度;中间态,应力与叶片速度成线性关系。发现颗粒和壁的粗糙度显着影响叶片混合器的流量。具有较高粗糙度的系统的特征在于增强的粒子运动和混合。在准静态状态下,单分散流观察到简单的比例关系。发现颗粒速度和扩散率与混合器尺寸和叶片速度成线性比例,而应力与颗粒床重量成线性比例。在多分散流中,发现由于筛分而发生尺寸偏析。然而,发现通过在最小和最大颗粒之间引入中间粒度可以降低偏析的程度。最后,检查了湿颗粒的流动。在低水分含量下,与干流相比,观察到了提高的颗粒速度和混合动力学。然而,在较高的水分含量下,观察到颗粒速度和混合速率降低。湿的颗粒流的特征在于颗粒附聚物的形成。附聚物的形成导致颗粒床粗糙度的增加,这极大地影响了宏观和微观流动特性。这些发现有助于理解复杂系统中的颗粒行为。更好地了解颗粒流将有助于开发基于第一性原理的模型,该模型可帮助设计和扩大叶片式搅拌机的运行并确定关键工艺参数。

著录项

  • 作者

    Remy, Brenda.;

  • 作者单位

    Rutgers The State University of New Jersey - New Brunswick.;

  • 授予单位 Rutgers The State University of New Jersey - New Brunswick.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2010
  • 页码 285 p.
  • 总页数 285
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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