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Numerical analysis of two-phase flow in condensers and evaporators with special emphasis on single-phase/two-phase transition zones

机译:冷凝器和蒸发器中两相流的数值分析,特别强调单相/两相过渡区

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摘要

A numerical study of the thermal and fluid-dynamic behaviour of the two-phase flow in ducts under condensation or evaporation phenomena is presented. The numerical simulation has been developed by means of the finite volume technique based on a one-dimensional and transient integration of the conservative equations (continuity, momentum and energy). The discretized governing equations are solved using the Semi-Implicit Method for Pressure-Linked Equations (SIMPLE) which allows back flow phenomena.\udSpecial emphasis is performed on the treatment of the transition zones between the single-phase and two-phase flow. The empirical inputs of single-phase and two-phase flow, including sub-cooled boiling\udand dry-out, have been adapted by means of adequate splines in the transition zones where the heat transfer correlations available in the literature are not suitable. Different numerical aspects have been evaluated with the aim of verifying the quality of the numerical solution. The mathematical model has been validated by comparison with experimental data obtained from literature considering condensation\udand evaporation processes. This comparison shown the improvements in the numerical solution not only in the transition zone but also in all condenser and evaporator ducts, when the special treatment for transitions\udis used. Illustrative results on double-pipe heat exchanger are also presented.
机译:给出了在冷凝或蒸发现象下管道中两相流热和流体动力学行为的数值研究。数值模拟是通过有限体积技术基于保守方程(连续性,动量和能量)的一维和瞬态积分而开发的。使用允许逆流现象的压力链接方程的半隐式方法(SIMPLE)求解离散的控制方程。\ ud特别强调处理单相和两相流之间的过渡区域。单相和两相流的经验输入,包括过冷的沸腾和干透,已经通过过渡区中的适当花键进行了调整,在过渡区中文献中可用的传热相关性不合适。为了验证数值解的质量,已经评估了不同的数值方面。该数学模型已经通过与从文献中考虑凝结\ udand蒸发过程的实验数据进行比较而得到验证。这种比较表明,当采用特殊的过渡处理方法时,不仅在过渡区域,而且在所有冷凝器和蒸发器管道中,数值解的改进。还介绍了双管换热器的说明性结果。

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