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Deterministic models to explain the phenomenon of interfacial mixing in refined products pipelines.

机译:确定性模型可以解释成品油管道中的界面混合现象。

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摘要

Understanding the processes governing axial dispersion of contaminants in a flowing system is one of the unsolved classical problems in fluid mechanics. Taylor (1953; 1954) provided a robust methodology to model such systems in their ideal laminar and turbulent flow conditions. The current study reveals that both laminar and turbulent conditions need to be considered simultaneously in order to accurately model axial dispersion in real systems. The analyses presented in this work provide a physical backing to Taylor's theory, while providing new conceptual visualizations of the processes governing axial dispersion. Theoretical and phenomenological analyses are carried out to show that the viscous sublayer has a significant role in axial dispersion under turbulent flow conditions.;A robust phenomenological model has been developed for estimating the axial dispersion coefficient for flow of liquids through straight pipes. The proposed model employs the viscous sublayer thickness as a parameter to combine the convective-diffusion equation with the boundary layer theory. The mathematical formulations developed using Reynolds analogy, in concurrence with the characteristic turbulent bursting events observed in the near-wall regions of the flow, have been shown to be applicable even for non-ideal low Reynolds number turbulent flow conditions. This hints at the possibility of a universal theory governing all mass, momentum, and heat transport processes. Furthermore, theoretical and empirical concepts used in pressure drop estimations for flow through straight and bent pipes have been demonstrated to be applicable to axial dispersion estimations. The axial dispersion models proposed in the current study have been validated using laboratory, pilot, and field experimental data. The proposed concepts could be used in identifying novel techniques to help reduce interfacial contamination in petroleum pipelines and other similarly affected processes. This work is also expected to lead to improved models and theories that broaden our understanding of the axial dispersion process.
机译:理解控制流动系统中污染物轴向扩散的过程是流体力学中尚未解决的经典问题之一。 Taylor(1953; 1954)提供了一种鲁棒的方法,可以在理想的层流和湍流条件下对此类系统进行建模。当前的研究表明,层流条件和湍流条件都需要同时考虑,以便准确地模拟实际系统中的轴向弥散。这项工作中提供的分析为泰勒理论提供了物理支持,同时提供了控制轴向弥散过程的新概念性可视化。理论和现象学分析表明,粘性子层在湍流条件下对轴向弥散具有重要作用。;已建立了鲁棒的现象学模型来估计液体通过直管的轴向弥散系数。该模型以粘性子层厚度为参数,将对流扩散方程与边界层理论相结合。与雷诺兹类比得出的数学公式以及在流动近壁区域中观察到的特征性湍流爆裂事件相一致,已被证明甚至适用于非理想的低雷诺数湍流条件。这暗示了一个普遍理论可以支配所有的质量,动量和热传递过程。此外,已经证明,用于直管和弯管的流量的压降估算中使用的理论和经验概念可应用于轴向弥散估算。当前研究中提出的轴向弥散模型已经使用实验室,中试和现场实验数据进行了验证。提出的概念可用于识别新技术,以帮助减少石油管道和其他类似过程中的界面污染。预计这项工作还将导致改进的模型和理论,从而拓宽我们对轴向弥散过程的理解。

著录项

  • 作者单位

    Oklahoma State University.;

  • 授予单位 Oklahoma State University.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2012
  • 页码 177 p.
  • 总页数 177
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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