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A hydrodynamic film model for fully developed, annular, horizontal two-phase pipe flow.

机译:用于完全展开的环形水平两相管道流的水动力膜模型。

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摘要

The objective of the present study was to develop a hydrodynamic model for fully-developed, annular, two-phase flows through horizontal pipes. The model is capable of describing local variations in the film thickness and local velocity profiles with respect to the radial and circumferential position within the pipe.; The study consisted of two parts: (1) development and solution of the mathematical model, the results of which are reported in the attached document, and (2) collection of experimental data on the film thickness for air-water flows in a 50.3 mm diameter horizontal pipe for Re{dollar}sb{lcub}rm g{rcub}{dollar} ranging from 47,000 to 202,000 and Re{dollar}sb1{dollar} ranging from 1,400 to 16,700. The actual collection of the experimental data was conducted jointly by the present author and by Mr. John Kitscha. Details of the experimental study are reported in (29). The experimental data from this study, along with experimental data from other investigators, was used to verify the mathematical model.; The resulting model is based on the direct solution of the local field equations using a finite difference approach. Unlike previously developed models, which involved integration of the field equations across the film boundary layer, the present model can describe the local hydrodynamic behavior as a function of radial, as well as circumferential position. The model is valid for superficial gas Reynolds numbers between 115,000 and 305,000, and for superficial liquid Reynolds numbers between 100 and 12,000. The model is valid for air-water flows as well as the flows of air and viscous liquids such as 50% glycerin. Agreement between the model and experimental data is good, with the errors between the predicted and experimental film thicknesses ranging between 5.9% and {dollar}-{dollar}29.6%.
机译:本研究的目的是为水平管道中完全展开的环形两相流建立水动力模型。该模型能够描述相对于管道内径向和圆周位置的薄膜厚度和局部速度分布的局部变化。该研究包括两个部分:(1)数学模型的开发和求解,其结果在所附文件中报告,以及(2)收集50.3 mm空气-水流膜厚度的实验数据Re {dollar} sb {lcub} rm g {rcub} {dollar}的水平管直径为47,000至202,000,而Re {dollar} sb1 {dollar}的直径范围为1,400至16,700。实验数据的实际收集是由本作者和John Kitscha先生共同进行的。实验研究的细节在(29)中有报道。该研究的实验数据以及其他研究者的实验数据被用于验证数学模型。所得模型基于使用有限差分法的局部场方程的直接解。与以前开发的涉及跨膜边界层的场方程积分的模型不同,本模型可以将局部流体动力学行为描述为径向以及圆周位置的函数。该模型适用于115,000至305,000之间的表观气体雷诺数,以及100至12,000之间的表观液体雷诺数。该模型适用于空气-水流以及空气和粘性液体(例如50%甘油)的流动。模型与实验数据之间的一致性很好,预测膜厚度与实验膜厚度之间的误差在5.9%至{29.6%之间。

著录项

  • 作者

    Jackman, Deborah Lynne.;

  • 作者单位

    The University of Wisconsin - Milwaukee.;

  • 授予单位 The University of Wisconsin - Milwaukee.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1992
  • 页码 245 p.
  • 总页数 245
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

  • 入库时间 2022-08-17 11:50:11

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