基于三阶剪切变形理论的悬臂输流管道自由振动

采用三阶剪切变形理论,结合有限元法研究了悬臂输流管道的自由振动问题．利用虚功原理建立了输流管系统的有限元方程,同时将悬臂端弹性支承以势能的形式引入到系统方程中,求解了系统前三阶的复频率．分别探讨了流体速度和弹簧刚度对系统复频率实部和虚部的影响,重点分析了弹簧刚度与前三阶固有频率间的关系．在弹性支承刚度为零的特例下,对比了本文结果与Timoshenko梁理论的结果,证明了本文方法的可靠性．研究发现系统固有频率的实部恒为负值,表明一端带有弹性支承的约束形式有利于提高悬臂输流管道自由振动的稳定性;流体的流动对管道振动起到了阻尼作用,在流动速度足够大的情况下,各阶振动固有频率均趋于零;当弹簧刚度为无穷大,且流体速度足够大时,输流管道将发生失稳．     

三参量固体模型粘弹性输流管道的动力特性分析

推导了三参量固体模型粘弹性输流管道的振动微分方程 ,计算了在不同无量纲松弛系数和弹性常数比下管道的无量纲临界流速和无量纲自振复频率 ,并给出了前三阶复频率与流速的关系 .计算结果表明 ,质量比、无量纲松弛系数及无量纲弹性常数比对输流管道的动力特性均有影响 .     

三参量固体模型粘弹性输液管道的动力特性分析

推导了三参量固体模型粘弹性输流管道的振动微分方程，计算了在不同无量纲松弛系数和弹性常数比下管道的无量纲临界流速和无量纲自振复频率，并给出了前三阶复频率与流速的关系。计算结果表明，质量比，无量纲松弛系数及无量纲弹性常数比对输流管道的动力特性均有影响。     

四边简支运动斜板热弹耦合稳定性研究

以四边简支运动斜板为模型,分析量纲为一的运动速度、长宽比、斜板角度以及热弹耦合系数等参数对运动斜板稳定性的影响。基于弹性薄板小挠度弯曲理论,利用Hamilton原理建立四边简支运动斜薄板的微分方程,采用微分求积法建立热弹耦合斜板的特征方程并进行求解,得到四边简支热弹耦合运动斜薄板的前三阶模态量纲为一的复频率随运动速度的变化曲线。相同条件下,一阶模态的发散失稳临界速度与量纲为一的热弹耦合系数的变化趋势一致,一阶模态发散失稳的临界速度随着斜板角度的增加而减小。     

非均匀随从力作用下热弹耦合圆环板的动力特性分析

基于弹性小挠度薄板理论和考虑变形的热传导方程,采用达朗贝尔原理建立了非均匀切向随从力作用下的轴对称圆环板热弹耦合运动方程。采用微分求积法推导了特征方程,得到内边简支(固支)外边自由边界条件下前三阶量纲为一复频率的实部和虚部随随从力的变化曲线;分析了随从力变化系数、热弹耦合系数、内外半径比对圆环板横向振动复频率和稳定性的影响。数值计算结果表明:在其它参数一定的情况下,圆环板发生第1阶和第2阶耦合颤振失稳;相应的颤振失稳临界载荷随着热弹耦合系数和内外半径比的增大而增大,但随着随从力变化系数的增大而减小。     

分析弹性支承输流管道的失稳临界流速

研究了两端弹性支承输流管道静态失稳和动态失稳临界流速. 根据梁模型横向弯曲振动模态 函数，由两端弹性支承的边界条件得到了其模态函数的一般表达式. 根据特征方程具体分析 了弹性支承刚度、质量比、流体压力和管截面轴向力等主要参数对失稳临界流速的影响. 数 值计算结果表明，管道在弹性支承下的动力稳定性比较复杂，在较小的弹性支承刚度和较小 的参数范围内，管道主要表现为动态颤振失稳；在较大的弹性支承刚度和较大的参数作用下， 管道的失稳形式主要表现为静态失稳；并且失稳临界流速随流体压力和管截面轴向压力的增 加而下降，随管截面轴向拉力的增加而上升.     

粘弹性地基上粘弹性输流管道的稳定性分析

从Winkler假设和单轴线性粘弹性本构方程出发，推导了Kelvin-Voigt粘弹性地基上三参量固体模型输流管道的运动微分方程，采用改进的有限差分法，分析了管道和地基的粘弹性参数对输流管道无量纲复频率和无量纲流速之间的变化关系的影响。     

运动车辆横向振动半车模型分析

通过半车模型, 数值研究平滑路面上运动车辆车体的前两阶横向振动频率. 将车体模型化为两端自由的Euler-Bernoulli梁, 半车模型的车轮模型化为两个弹性不等的弹簧. 建立半车模型的数学模型描述车体的横向振动. 以两端自由的静态梁的模态为试函数和权函数, 通过高阶Galerkin截断计算车体横向振动的频率, 并研究车辆运行速度、车体刚度、弹簧刚度等参数对车体振动频率的影响.     

两端弹性支承输流管道固有特性研究

输流管道广泛应用于航天航空、石油化工、海洋等重要的工程领域, 其振动特性尤其是系统固有特性一直是国内外学者研究的热点问题. 本文研究了两端弹性支承输流管道横向振动的固有特性, 尤其是在非对称弹性支承下的系统固有特性. 使用哈密顿原理得到了输流管道的控制方程及边界条件, 通过复模态法得到了静态管道的模态函数, 以其作为伽辽金法的势函数和权函数对线性派生系统控制方程进行截断处理. 分析了两端对称支承刚度、两端非对称支承刚度、管道长度以及流体质量比对系统固有频率的影响规律, 重点讨论了管道两端可能形成的非对称支承条件下固有频率的变化规律. 结果表明, 较大的对称支承刚度下管道的第一阶固有频率下降较快; 当管道两端支承刚度变化时, 管道的各阶固有频率在两端支承刚度相等时取得最值; 对于两端非对称支承的管道而言, 两端支承刚度越接近, 第一阶固有频率下降的越快, 而且相应的临界流速越小; 流体的流速越大, 其对两端非对称弹簧支承的管道固有频率的影响更为明显.      

传递矩阵法分析约束悬臂裂纹管道失稳临界流速

研究了自由端受线性弹簧支承和扭转弹簧约束的悬臂输流管道在含有圆周非贯穿裂纹时的失稳临界流速;根据梁模型模态函数的一般表达式和裂纹处的关联式以及传递矩阵法推导出含裂纹梁的模态函数;根据特征方程具体分析了裂纹位置、裂纹深度、裂纹圆周角等参数对系统失稳临界流速的影响,并进行了数值仿真分析。结果表明:由于裂纹的存在,系统的失稳临界流速下降,动态失稳临界流速下降的速率和幅值均比静态失稳临界流速下的大;临界流速与裂纹位置、深度和裂纹圆周角等参数密切相关,特别是对颤振失稳临界流速的影响更明显,在裂纹位置、裂纹非贯穿圆周角、裂纹深度等参数影响下,管道的失稳形态将从屈曲失稳转变为颤振失稳。     

Resistance in the core flow of a fiber suspension in a tube

Using a more simple formulation than that of [1], the problem of core flow of a fiber suspension in a straight tube of circular cross section is considered. The solution is sought by the small parameter method. The first approximation thus found is compared in detail with experiment. Formulas are obtained for the tube resistance coefficient and the dimensionless thickness of the near-wall layer. The laminar flow in the first approximation is characterized by three dimensionless complexes. Both the resistance coefficient and the dimensionless thickness of the near-wall layer depend on only two of the complexes, and so partial simulation of the flow is possible.     

The cross-flow heat exchanger in comparison

As shown in a former paper, the dimensionless mean temperature difference for the cross-flow characteristic is only a function of two independent dimensionless variables. Each of it is defined by the conditions of one of the two interacting streams. The dimensionless mean temperature difference but also can be used as a scale for a comparison of the different flow characteristics, when only the flow characteristic is changed and all other conditions of the interacting streams remain constant. For the flow characteristics of the parallel-flow as well as of the counter-flow, here additionally the dimensionless mean temperature differences are derived as a function of the two independent dimensionless variables for the interacting streams, with which now an immediate comparison of all three flow characteristics can be done.     

An asymptotic solution for fluid production from an elliptical hydraulic fracture at early-times

The early-time transient flow during the start-up of fluid production from a porous medium by a well intersected by a vertical elliptical hydraulic fracture is studied using an asymptotic analysis. The analysis is focused on the situation of practical interest where the fracture conductivity is high so that production from the fracture dominates. The first three terms in a short-time asymptotic expansion for the production rate during constant-pressure production, and for the well-pressure during constant-rate production, are obtained. It is shown that the fracture tip starts to influence the production rate only when the dimensionless time is increased to the square of the reciprocal of the dimensionless fracture conductivity. The asymptotic results also show that geometric factors of an elliptical fracture introduce non-negligible corrections to the so-called bilinear flow in the early times, which were previously erroneously associated with the effect of the fracture tip.     

Stability analysis of viscoelastic curved pipes conveying fluid

Based on the Hamilton' s principle for elastic systems of changing mass, a differential equation of motion for viscoelastic curved pipes conveying fluid was derived using variational method, and the complex characteristic equation for the viscoelastic circular pipe conveying fluid was obtained by normalized power series method. The effects of dimensionless delay time on the variation relationship between dimensionless complex frequency of the clamped-clamped viscoelastic circular pipe conveying fluid with the Kelvin-Voigt model and dimensionless flow velocity were analyzed. For greater dimensionless delay time, the behavior of the viscoelastic pipe is that the first, second and third mode does not couple, while the pipe behaves divergent instability in the first and second order mode, then single-mode flutter takes place in the first order mode.     

弹性地基上转动FGM梁自由振动的DTM分析

基于Euler-Bernoulli梁理论,利用广义Hamilton原理推导得到弹性地基上转动功能梯度材料(FGM)梁横向自由振动的运动控制微分方程并进行无量纲化,采用微分变换法(DTM)对无量纲控制微分方程及其边界条件进行变换,计算了弹性地基上转动FGM梁在夹紧-夹紧、夹紧-简支和夹紧-自由三种边界条件下横向自由振动的无量纲固有频率,再将控制微分方程退化到无转动和地基时的FGM梁,计算其不同梯度指数时第一阶无量纲固有频率值,并和已有文献的FEM和Lagrange乘子法计算结果进行比较,数值完全吻合。计算结果表明,三种边界条件下FGM梁的无量纲固有频率随无量纲转速和无量纲弹性地基模量的增大而增大;在一定无量纲转速和无量纲弹性地基模量下,FGM梁的无量纲固有频率随着FGM梯度指数的增大而减小;但在夹紧-简支和夹紧-自由边界条件下,一阶无量纲固有频率几乎不变。     

Unsteady convective mass transfer in a three-zone system

A three zone unsteady state mass transfer problem is considered for flow between parallel plates. Solute is transferred from the moving zone to the other two, in one of which a first order reaction consuming the solute occurs. (An industrially important example of this situation would be the absorption of a gas from a lean mixture into a liquid-saturated ion exchange membrane.) The double Laplace transformation is applied to the system equations. In obtaining the inversion of the transformed equations the first inversion (with respect to the transformed dimensionless axial distance) is performed by use of the residue method, and then the second inversion (with respect to the transformed dimensionless time) is performed by use of the numerical technique developed by Bellman et al. Some numerical results are presented and discussed.     

Dynamics of cantilevered pipes conveying fluid. Part 1: Nonlinear equations of three-dimensional motion

In a three-part study, the first part being this paper, the investigation of the three-dimensional nonlinear dynamics of unrestrained and restrained cantilevered pipes conveying fluid is undertaken. The full derivation of the equations of motion in three dimensions for the plain cantilevered pipe is presented first in this paper, using a modified version of Hamilton's principle, adapted for an open system. Intermediate (between the clamped and free end) nonlinear spring constraints are then incorporated into the equations of motion via the method of virtual work. Furthermore, a point mass fixed at the free end of the pipe is also added to the system. The equations of motion are presented in dimensionless form and then discretized with Galerkin's method.     

Pressure drop in two phase slug/bubble flows in mini scale capillaries

A segmented two phase slug/bubble flow occurs where a liquid and a gas are pumped into the same tube over a range of Reynolds numbers. This segmented two phase flow regime is accompanied by an increase in pressure drop relative to the single phase flow where only one fluid is flowing in a capillary. This work experimentally and theoretically examines the pressure drop encountered by the slug/bubble flow with varying slug lengths in mini channels. In the experimental work the dimensionless parameters of Reynolds number and Capillary number span over three orders of magnitude, and dimensionless slug length ranges over two orders of magnitude to represent flows typical of mini- and micro-scale systems. It is found, in agreement with previous work, that these dimensionless groups provide the correct scaling to represent the pressure drop in two phase slug/bubble flow, although the additional pressure drop caused by the interface regions was found to be ∼40% less than previously reported.