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A computational model for swirl vane phase separators

机译:旋流叶片相分离器的计算模型

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摘要

The main objective of this study is to develop a mechanistic separator-dryer model for the TRAC-BF1 code to solve the problems associated with the modeling of the steam separation phenomena. This model, in a sense, is an extension to the existing separator-dryer model in the TRAC-BF1 code. The phasic velocities and the pressures for the vapor core and the liquid film regions of the swirl vane separator are solved by the use of phasic mass and momentum equations along with pressure drop. A new dryer efficiency model is also introduced. In this model, the dryer efficiency is calculated by the corrugated plate efficiency model. The important part of the study focuses on the implementation of the separator-dryer model to the code. The implementation uses the correct convective parameters in the solution of the conservation equation for the mixing cell of separator-dryer component.;The model is tested and assessed against the experimental data, an actual reactor transient, and the results of the existing model. The results indicates that the new steam separation model is more accurate and more robust when compared to the separator-dryer model.
机译:这项研究的主要目的是为TRAC-BF1代码开发机械分离器-干燥器模型,以解决与蒸汽分离现象建模相关的问题。从某种意义上说,该模型是TRAC-BF1代码中现有分离干燥器模型的扩展。通过使用相位质量和动量方程式以及压降来求解旋流叶片分离器的蒸气芯和液膜区域的相速度和压力。还介绍了新的干燥机效率模型。在此模型中,烘干机效率是通过瓦楞纸板效率模型计算的。研究的重要部分集中于对代码执行分离器-干燥器模型。该实现在分离器-干燥器组件的混合单元的守恒方程的解中使用了正确的对流参数。该模型是根据实验数据,实际反应堆瞬变以及现有模型的结果进行测试和评估的。结果表明,与分离器-干燥器模型相比,新的蒸汽分离模型更准确,更可靠。

著录项

  • 作者

    Lider, Serhat.;

  • 作者单位

    The Pennsylvania State University.;

  • 授予单位 The Pennsylvania State University.;
  • 学科 Nuclear engineering.;Mechanical engineering.
  • 学位 Ph.D.
  • 年度 1997
  • 页码 142 p.
  • 总页数 142
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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