气液两相瞬变流的流固耦合模型研究

传统的气液两相流瞬态分析和管道动力响应计算是分开的，存在一定的缺陷．针对石油工业中常见的多相混输问题，介绍了常见的气液两相流瞬态模型和流固之间存在的耦合机理，在不作薄壁管假设的前提下推导出了气液两相瞬变流的流固耦合模型．与现有相似模型的对比分析表明，这一模型比较全面地考虑了流体和管道的特性以及不同的耦合形式，可以适应实验和／或仿真研究的需要．     

气液两相流中旋涡诱发圆柱振动时的脉动升力研究

一定条件下 ,垂直上升矩形截面管内的气液两相流横向冲刷水平布置的圆柱时 ,圆柱在与来流垂直的水平方向上受到了脉动升力的作用。本文在 1.6× 10 4到 6 .0×10 4的 Re数范围和 0到 0 .32的来流含气率范围内 ,进行了实验研究。实验中 ,流体工质为由空气和水混合而成的泡状流 ,采用弹性梁 -电阻应变式小力值传感器来测量圆柱受到的脉动升力 ,利用计算机对传感器的输出信号进行连续采集 ,采集频率为5 0 0 Hz。对由实验得到的脉动升力数据进行自功率谱分析 ,得出在两相流中只有在小于 0 .10～ 0 .12的来流含气率范围内 ,圆柱后部才会形成涡街 ,且此时的 Strouhal数随来流含气率的增大而增大 ;由脉动升力数据的均匀方根值算出脉动升力系数 C′L发现小 Re数时 C′L 随来流含气率的增大而增大 ,而在大 Re时 C′L 随来流含气率的增大先稍下降后再增大。     

分块法研究圆柱绕流升阻力

使用新的分块耦合方法，分别对单圆柱和串列双圆柱绕流进行了数值模拟．对于单圆柱绕流，低Re下计算所得到的定常涡尺寸与实验非常接近．对于串列双圆柱绕流，研究分析了改变双圆柱中心间距对上下游圆柱的升阻力系数和脉动频率所产生的影响，计算结果与实验非常吻合，为进一步研究涡致振动提供了依据．     

圆柱绕流的非线性动力学全局性太分析

针对圆柱绕流个具体问题，利用Galerkin方法得到了与之相应的离散化的动力学系统，确定了该离散化系统的所有无穷远奇点及其稳定性，为进一步深入研究圆柱绕流动力学性太提供了基础。     

圆柱绕流的非线性动力学全局性态分析

针对圆柱绕流这个具体问题，利用Ｇａｌｅｒｋｉｎ方法得到了与之相应的离散化动力学系统。确定了该离散化系统的所有无穷远奇点及其稳定性，为进一步深入研究圆柱绕流动力学性态提供了基础。     

分块法研究圆柱绕流升阻力

 使用新的分块耦合方法，分别对单圆柱和串列双圆柱绕流进行了数值 模拟. 对于单圆柱绕流，低$Re$下计算所得到的定常涡尺寸与实验非常接近. 对于 串列双圆柱绕流，研究分析了改变双圆柱中心间距对上下游圆柱的升阻力系数和脉动频率所 产生的影响，计算结果与实验非常吻合，为进一步研究涡致振动提供了依据.     

单层偏心圆柱薄壳的自由振动特性分析研究

本文从偏心圆柱壳截面的几何特性出发,将偏心圆柱壳问题转化为一个周向变厚度圆柱壳问题,随后利用其状态向量之间的传递矩阵将壳体的振动控制方程转化为矩阵微分方程形式,通过Magnus级数法求解传递矩阵得到频率方程。采用Lagrange插值法得到偏心圆柱壳体自由振动状态下的固有频率,并且与圆柱壳的固有频率进行了比较。对影响结构固有频率的主要参数进行了分析,得到了这些参数和固有频率之间的关系。本文不仅提出了一种有效求解偏心圆柱壳固有频率的新方法,同时亦可为检测偏心圆柱壳的偏心距提供一种新的思路和方法。     

圆柱绕流三维不稳定性的低维Galerkin法分析

利用低维Ｇａｌｅｒｋｉｎ方法及Ｆｌｏｑｕｅｔ稳定性分析理论,计算分析了圆柱绕流的三维线性不稳定性．分析中构造了能较好描述尾迹区流动的周向基函数,建立了完备的合理的基函数组,改进了计算机算法．结果证实圆柱二维周期流对展向小扰动为不稳定的,正确地预计了出现三维长波不稳定性的临界雷诺数Ｒｅｃ＝１９０;扰动展向波长为λｃ一３．６ｄ．对雷诺数Ｒｅ为１８０,１９０两种工况下的圆柱三维绕流流场的计算进一步证实了这种流动的整体不稳定性．本文所预计的临界值比Ｎｏａｃｋ等人的结果更为精确,与Ｂａｒｋｌｅｙ等人的ＤＮＳ解一致,与Ｗｉｌｌｉａｍｓｏｎ的实验相符．     

FBRE系统偏心力下的功率流特性及主动控制

利用机械阻抗方法推导了偏心力作用下，机器－隔振器－柔性板基础所组成的FBRE隔振系统的动态传递方程。以传递到柔性板基础的功率流为目标函数，通过计算机仿真计算，研究了在对称系统中偏心力作用下的功率流特性，分析了和对称力、力矩作用效果的不同和联系，并探讨了主动控制策略的效果。     

滑动表面卷吸速度为零时的热弹流润滑分析

提出了接触处两表面等速反向运动的圆柱间在一定条件下赤存在足够厚的稳态热弹流膜,此时固体表面呈现中凹状、且凹陷深度随勒荷的增加而增大,随表面速度的增加而减小。     

Flow of Robertson-Stiff fluids through an eccentric annulus

I.IntroductionInthepetroleumindustry,itisusuallythecasethatthedrillingstring(orcasingpipe)isnotlocatedinsidethecenteroftheflowgeometryduringdrillingandcompletillgpl'ocess,this,inturll,willaltertile'11owingbehaviorofdrillingmudandcementslurl.ieswhichtlowinginaneccentricallllulus.OilaccoUlltofviscousofnon-Newtoniantluid,flowillaneccentricannulusdifTeresmuchwiththatinacollcentricannulus.Mailyinvestigatorshaveconductedresearchworksonthisstlbject.Earlyin1935,TaoandDollovallrealizedthattheimpel.t…     

大间隙环流壁面摩擦及偏心转子静特性研究

基于紊流整体流动模型和Ｍｏｏｄｙ壁面摩擦系数方程简化了大间隙环流三维流非线性偏微分控制方程组,推导了零阶摄动方程并采用数值方法对大间环流中偏心转子静特性进行了深入研究。实例计算结果表明：大间隙环流中转子与以灿承和密封为代表的小间隙环流中转子的静特性有很大同;壁面摩擦系数沿周向变化,同时转子和静子壁面粗糙度以及偏心率对大间隙环流中转子静特性有较大的影响。     

环形截面螺旋管道内二次流动特性的研究

从曲线柱坐标系下的N-S方程出发,以曲率和挠率为小参数,采用摄动法求解了环形截面螺旋管道内的黏性流动,给出了完全二阶摄动解,结果表明：当挠率为零时,二次流表现为上下对称的四个涡;当挠率不为零,涡的对称性遭到破坏,二次涡的强度和个数受De数和环形截面内外径之比δ的影响,轴向速度最大值在De数较小时靠近管道的内侧,随着De数的增加,其最大值向外侧移动。     

粗糙度对大间隙环流偏心转子动特性系数的影响

基于作者建立的大间隙环流中转子运动的理论模型,用摄动法推导了大间隙环流流场非线性控制方程的一阶摄动方程,采用数值方法研究了静子和转子壁面粗糙度对大间隙环流中偏心转子动特性系数的影响。研究结果表明：静子和转子壁面粗糙度对大间隙环流中偏心转子动特性系数有较大影响。所得到的数值结果与已有的解析解和实验结果具有较好的一致性。     

Analytical solutions of the helical flow of non newtonian fluid in eccentric annular space

ＡＮＡＬＹＴＩＣＡＬＳＯＬＵＴＩＯＮＳＯＦＴＨＥＨＥＬＩＣＡＬＦＬＯＷＯＦＮＯＮＮＥＷＴＯＮＩＡＮＦＬＵＩＤＩＮＥＣＣＥＮＴＲＩＣＡＮＮＵＬＡＲＳＰＡＣＥＺｈａｎｇＨａｉ－ｑｉａｏ（张海桥）ＷｕＪｉ－ｚｈｏｕ（吴继周）（ＴｈｅＤｅｐａｒｔｍｅｎｔｏｆ...     

STEADY FLOW IN A CURVED PIPE WITH A COAXIAL CORE

In this paper we study the steady annular flow of a viscous fluid into an annular pipe and discuss the effects of the size of the core on the flow properties.     

Entrance flow in eccentric annular ducts

A control-volume-based solution of the complete set of Navier-Stokes equations for the laminar, three-dimensional developing flow in straight, eccentric, cylindrical annular ducts is described. Numerical results for velocity and pressure development, pressure defect and entrance lengths are presented for a wide range of duct parameters, i.e. relative eccentricity ? and radius ratio γ. The present results match very well with earlier numerical solutions for the limiting cases of developing flow in concentric ducts and fully developed flow in eccentric ducts. Comparison with earlier approximate results for developing flow in eccentric ducts indicates that the approximate model predicts the velocity and pressure development with an error of about 10%. However, the development length predicted by the approximate model is grossly in error. The pressure defect and development length in eccentric ducts are very high compared with their counterparts in concentric ducts. The pressure defect, development length and maximum velocity increase with the radius ratio for eccentric ducts, while the reverse is true for concentric ducts. Also, the apparent friction factor decreases as the eccentricity increases.     

VIBRATION AND STABILITY OF VERTICAL UPWARD-FLUID-CONVEYING PIPE IMMERSED IN RIGID CYLINDRICAL CHANNEL

A theoretical model is developed for the vibration and stability of a vertical pipe subjected concurrently to two dependent axial flows. The external fluid, after exiting the outer annular region between the pipe and a rigid cylindrical channel, is conveyed upwards inside the pipe. This configuration thus resembles of a pipe that aspirating fluid. The equation of planar mo- tion is solved by means of the differential quadrature method （DQM）. Calculations are conducted for a slender drill-string-like and a bench-top-size system, for different confinement conditions of the outer annular channel. It is shown that the vibrations of these two systems are closely related to the degree of confinement of the outer annular channel. For a drill-string-like system with narrow annuli, buckling instability may occur in the second and third modes. For a bench-top-size system, however, both buckling and flutter may occur in the lowest three modes. The form of instability depends on the annuli size.     

Effect of drag reducing polymer on air–water annular flow in an inclined pipe

Drag reduction (DR) for air and water flowing in an inclined 0.0127 m diameter pipe was investigated experimentally. The fluids had an annular configuration and the pipe is inclined upward. The injection of drag reducing polymer (DRP) solution produced drag reductions as high as 71% with concentration of 100 ppm in the pipeline. A maximum drag reduction that is accompanied (in most cases) by a change to a stratified or annular-stratified pattern. The drag reduction is sensitive to the gas and liquid superficial velocities and the pipe inclination. Maximum drag reduction was achieved in the case of pipe inclination of 1.28° at the lowest superficial gas velocity and the highest superficial liquid velocity. For the first time in literature, the drag reduction variations with the square root of the superficial velocities ration for flows with the same final flow patterns have self-similar behaviors.     

大间隙环流中偏心转子动特性系数的数值分析方法

基于作者用整体流动理论和Moody壁面摩擦系数方程建立的大间隙环流中转子动特性系数数值计算模型,应用摄动方法推导了大间隙环流流场非线性控制方程组的一阶摄动方程,提出了求解大间隙环流中偏心转子动力学特性系数的数值分析方法。用该方法得到的数值结果与已有的解析解和实验结果具有较好的一致性。