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A study of powder making by the decomposition of nickel carbonyl in an aerosol tube reactor.

机译:在气溶胶管反应器中通过羰基镍分解制粉的研究。

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摘要

In this study, nickel carbonyl decomposition in a hot wall tube reactor was investigated using mathematical modeling and experimental observations.; A simple first principles approach was used to develop a model for particle growth inside the reactor. The mass balance was composed from published mechanisms and constants for the simultaneous homogeneous and heterogeneous decomposition of nickel carbonyl. The particle population balance was constituted using a general expression for Brownian coagulation, which is valid across the range of particle size. The model assumed that the particle size was monodisperse, coalescence was immediate and that the reactor was plugflow. The model predicted a rapid nucleation burst, followed by surface reaction and an asymptotic increase in particle size.; The reactor in this study was equipped with samplers that extracted samples at S axial positions and 3 radial positions during the reaction. Special care in the design and operation of these samplers insured that thermophoresis was the dominant mode of particle collection. Each of the samples was measured by an appropriate microscope technique and the particles were sized and counted by image analysis. These measurements were converted into particle size distributions, and particle number concentrations to obtain detailed snapshots of the particle evolution at all points within the reactor.; In this study, nucleation occurred within 0.14 seconds or less. Particles grew extremely quickly by the surface reaction, to a size of 20--30 nm and a number concentration of 1015--1016 particle/gram of gas. These particles continued to grow by coagulation. As this happened, nucleation briefly continued, which created a temporary bimodal distribution, that persisted as residual nickel carbonyl gas was available. When the carbonyl gas became depleted, the bimodal distribution was transformed to a log-normal distribution by coagulation and approached the self-preserving limit. The simple aerosol model developed earlier described the experimental results well when the size distribution was log-normal, but not so well when the distribution was strongly bimodal.
机译:在这项研究中,使用数学模型和实验观察研究了热壁管式反应器中羰基镍的分解。使用一种简单的第一原理方法来开发反应堆内部颗粒生长的模型。质量平衡由公开的机理和常数组成,用于同时羰基镍的均相和非均相分解。使用布朗凝聚的一般表达式构成粒子种群平衡,该表达式在整个粒度范围内均有效。该模型假定粒径为单分散,立即聚结,反应器为塞流。该模型预测成核迅速爆发,随后发生表面反应,粒径逐渐增加。本研究中的反应器配备有采样器,可在反应过程中在S轴向位置和3个径向位置提取样品。这些采样器的设计和操作中要特别小心,以确保热泳是颗粒收集的主要方式。通过适当的显微镜技术测量每个样品,并通过图像分析确定颗粒的大小和计数。将这些测量值转换成粒度分布和颗粒数浓度,以获得反应器内所有点处颗粒演化的详细快照。在这项研究中,成核发生在0.14秒或更短时间内。颗粒通过表面反应非常迅速地生长,尺寸达到20--30 nm,气体浓度为1015--1016颗粒/克。这些颗粒通过凝结继续生长。发生这种情况时,成核作用短暂地继续,这产生了暂时的双峰分布,并在残留羰基镍气体存在时持续存在。当羰基气体耗尽时,双峰分布通过凝结转变为对数正态分布,并达到自保存极限。当尺寸分布为对数正态分布时,较早开发的简单气溶胶模型很好地描述了实验结果,但当分布为强双峰分布时,效果不佳。

著录项

  • 作者

    Wasmund, Eric Bain.;

  • 作者单位

    McMaster University (Canada).;

  • 授予单位 McMaster University (Canada).;
  • 学科 Engineering Materials Science.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 268 p.
  • 总页数 268
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 工程材料学;
  • 关键词

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