超急速爆发沸腾的傅立叶与小波分析

采用快速瞬态微型压力测量系统对脉冲激光加热下无水乙醇超急速爆发沸腾过程中液池内压力变化进行了测量,利用傅立叶变换、小波分析等理论工具对该过程的能量与频率特性进行了分析,并对汽泡群行为进行了理论推测.结果发现,爆发沸腾过程中压力信号频率处于MHz量级;在不同阶段气泡群行为具有不同特点.     

输油管道对流换热系数模型

热油管道能耗巨大,其散热问题的研究具有极高的工程应用价值。尽管在很多情况下流体与管壁间的对流换热系数很大,可以在总传热系数计算中忽略对流换热系数的影响,但并不总是如此。主流与近壁边界间的过渡区、即热边界层内的换热是不可忽略的。采用动量热量比拟的方法建立输油管道对流换热系数模型,并在此基础上对总传热系数进行了分析计算。计算结果表明,边界层内的对流换热系数对管道的总传热系数具有较大影响。     

爆发沸腾形核及压力模拟

对爆发沸腾形核阶段的微观过程进行了分析与描述,运用分子势能模型并结合经典形核功理论计算得到临界气泡半径;针对形核与气泡生长阶段功量的重要影响因素--压力,采用Ls-Dyna显示动力学软件对爆发沸腾过程的压力分布进行了模拟分析.     

Fourier and Wavelet Transform Analysis of Pressure Signals during Explosive Boiling

The transient pressure in a liquid-pool during explosive boiling of acetone is measured by a micro-pressure-measuring system. The Fast Fourier transform and continuous wavelet transform methods are applied to investigate the frequency characteristics. The results show that the dominant frequency of the explosive boiling is 0-2 MHz, and the bubble cluster formed by numerous tiny bubbles departs twice. Analysis and discussions are also conducted to explain the bubble evolution during the explosive boiling.     

油气混输管道段塞流稳态计算模型

在石油工业中油气混输管道中的段塞流的水力计算一直是多相流管道稳态工艺计算中的难点。本文在总结国内外相关研究成果的基础上提出了一种基于段塞流结构参数的计算方法。计算结果表明,该模型能够对段塞流的压力梯度进行模拟,在油气混输管道的水力计算方面具有实用价值。     

A Novel Kinetic Model of Liquid Nitrogen＇s Explosive Boiling at the Initial Stage

The liquid nitrogen＇s explosive boiling characteristics under transient high heat flux have attracted increasing attentions of researchers over the world due to its wide applications. Although some experiments have been performed, the process and the characteristics at the initial stage, especially within 1 ~s, have not been described reasonably yet. Based on the related experiments and theoretical analysis, a novel kinetic model combined with quasi-fluid idea is presented to analyse the characteristics of liquid nitrogen＇s explosive boiling at the initial stage. The results indicate that the model can appropriately describe the liquid nitrogen＇s explosive boiling. The behaviour and the heat transfer characteristics of a single bubble are very different from those of the bubble cluster, thus the behaviour of individual bubbles could not be directly applied to describe the explosive boiling process at the initial stage.