考虑滩地植被的复式断面河道水流的二维解析解

针对滩地植被化的复式断面河道的水流特性,从沿水深积分的紊流时均运动微分方程出发,基于恒定均匀流的假设,给出了植被作用下河道水流水深平均流速沿横向分布的二维解析解.其中,将植被对水流的影响归结为拖曳力项,在模型中计及了二次流的影响,并对二次流强度系数K的取值进行了初步探讨.分别对顺直河道横断面和蜿蜒河道的顶点断面进行了计算,计算结果与试验资料符合良好,表明给出的二维解析解可用于植被作用下复式断面河道水流水深平均流速沿横向分布的数值预报.     

部分植被化矩形河槽紊流时均流速分布分析解

研究了部分植被化矩形河槽紊流的水深平均流速分布．植被被视为不可移动的刚性多孔介质,植被对水流的阻力以多孔介质理论加以考虑,并综合考虑部分植被存在时矩形河槽紊动水流二次流的作用,建立了紊流动量方程．针对恒定均匀流的特点,对动量方程进行了简化,沿水深方向积分并引入参考量,形成无量纲形式的基于多孔介质理论紊动水流控制方程,进而对其求解给出了水深平均纵向时均流速分布的分析解．研究表明,在不同水流条件下的二次流强度系数具有相同的数量级．为验证分析解的正确性,在实验室采用MicoADV测量了部分植被化矩形河槽水流的流速分布．数值解与实验资料和日本学者的相关实验资料的对比表明,该方法可以准确预测部分植被化矩形河槽紊流水流的水深平均流速分布．     

粗颗粒高含沙两相紊流运动规律的实验研究

本文通过在矩形断面水平管道中的输沙试验,研究了粗颗粒二相高含沙水流的流速及含沙浓度分布。在主流区,流速分布遵从对数规律,卡门常数则为利查逊数及浓度的函数。底床附近,流速分布受到升力效应的影响。管道高含沙水流的悬沙浓度分布与明渠低含沙水流大不相同,利用扩散方程求出浓度分布公式,与实测结果符合得很好。     

相似理论和泥沙的垂直分布

本文利用相似性原理处理了二维渠道均匀定常挟沙水流,在湍流脉动速度和含沙量涨落值相似的条件下,我们得到了泥沙垂直于挟沙水流的流动方向的含沙量分布.这个含沙量分布和扩散理论得到的含沙量分布略有差别,而和重力理论得到的含沙量分布则差别较大.     

高含沙水流的水流结构及运动机理

本文在室内水槽试验和天然河流资料分析的基础上,对含有一定细颗粒泥沙(d₅₀<0.01mm)的高含沙水流进行了分析研究.对高含沙水流的类型、宾汉切应力τ_B和刚性系数η的性质、流核与非流核区的水流运动机理和切力分布等都提出了作者的见解,对二维恒定均匀紊流的高含沙水流的流速分布提出了计算公式,公式既适用于高含沙宾汉流体,也适用于清水和高含沙牛顿流体.     

有限体积KFVS方法在二维溃坝中的应用

本文采用了基于KFVS格式的有限体积方法 (FVM)求解了控制水流运动的二维浅水方程 ,建立了二维水坝瞬间溃坝的洪水演进模型 .并应用此模型模拟了二维非对称溃坝和对称溃坝情形下坝左下角有障碍物时的洪水波演进过程 .模拟结果表明该数学模型对二维浅水运动的模拟很有效 .     

基于二次插值的非饱和土壤水流问题的特征差分方法及数值模拟

本文针对一类非饱和土壤水流问题,提出了基于二次插值的特征差分格式,得到了严谨的L2模误差估计.并作了数值试验,指明方法的有效性.     

泥沙对水的相对速度和含沙浓度对脉动速度的影响

本文从流体动力学的基本理论出发,讨论了泥沙运动理论中的三个基本问题.(1)泥沙在湍性水流中对水的相对速度.(2)水流挟带泥沙以后脉动速度的改变.(3)泥沙在二维渠道均匀定常流动中含沙量的垂直分布和通常的扩散理论的修正.按照我们理论分析的结果,发现和通常水力学及河道动力学中常用的表达式有一些出入.     

二维非饱和水流的全离散广义差分格式分析及其数值模拟

建立二维非饱和水流问题的全离散广义差分格式,讨论了全离散广义差分解的存在唯一性,并给出最优误差估计的证明．最后给出数值算例,验证方法的有效性.     

一个综合植被地表径流与饱和地下水流之间相互作用的数值模型

构建一个综合的数值模型,用来处理植被地表径流与饱和地下水流之间的相互作用问题.综合了早先提出的准三维植被地表径流模型,与二维饱和地下水流模型建立起该数值模型.植被地表水流模型被构建为,二维浅水方程(SWE)显式的有限体积解,耦合了Navier-Stokes方程(NSE)隐式的有限差分解,得到了竖向速度的分布.地下水流模型是以二维饱和地下水流方程(SGE)显式的有限体积解为基础构建.通过在连续方程中引入源-汇项,达到植被地表径流和地下水流之间的相互作用.单一的规则将2个解紧密地耦合在一起.最后,应用4个案例来验证本综合模型,结果是令人满意的.     

泥石流固液分相流速计算方法研究

泥石流固液分相流速是泥石流对岸坡、防治结构冲击、磨损机理的核心问题．将泥石流体简化为具有相同粒径的固相和具有相同力学性质的液相,基于泥石流体为沿流动方向的一维两相流体,运用两相流理论建立了泥石流固液分相流速控制方程．构建了泥石流平均压力、彻体力及平均表面力的计算方法,尤其通过浆体的Binhanm体流变方程、Bagnold颗粒相互作用试验成果建立了控制体平均表面力计算方法;建立了固液两相流速比例系数,以及理论固相流速与实际流速的比例系数．据此求解控制方程得到了固液分相流速计算方法,该方法既可同时适用于粘性泥石流和稀性泥石流,也可在泥石流爆发以后通过现场采集沉积物分析反求泥石流爆发期间的分相流速．工程实例分析显示,该方法计算结果与实测结果吻合较好．     

Mush–Chimney Convection

Mush–chimney convection occurs in a system consisting of a layer of mixed solid and liquid bounded by liquid above and solid below. The solid phase of the mush is composed of the denser constituent of the alloy, making the residual liquid compositionally buoyant as solidification proceeds. The liquid is in steady, nonlinear convection, consisting of a downward flow in the mush and an upward flow in a chimney, free of solid, which formed spontaneously in the mush as a result of the interaction between flow and structure. A well-posed continuum mathematical model of this system is developed. A novel feature of this analysis is the development of an equation that determines the chimney radius. Material diffusion is an essential ingredient in this equation, but is negligible elsewhere. In the parameter range considered, the problem is well posed without the necessity of specifying the condition of marginal phase equilibrium. A remarkably simple analytic solution is obtained for the convective flow in the chimney.     

Steady and Unsteady Jet Wiping Processes

The jet wiping process is widely used in continuous coating applications to remove the excess amount of liquid entrained by a sheet moving out of a liquid bath. Typical fields of applications are hot dip galvanization of metal strips and coating of photographic films. The process is based on the impact of a gas jet onto the liquid film carried by the solid substrate. In the present study the process is investigated for the case of strictly two‐dimensional flow. It is assumed that inertia effects on the film flow can be neglected, whereas the effects of the pressure gradient and the shear stress distribution of the impinging jet and the surface tension of the liquid film are taken into account. As a result it is possible to derive a single kinematic wave equation which governs the distribution of the film thickness. Numerical results for representative steady and unsteady processes including the formation of shock discontinuities are presented.     

Computer simulations of sodium formate solution in a mixing tank

Traditionally, solid–liquid mixing has always been regarded as an empirical technology with many aspects of mixing, dispersing and contacting were related to power draw. One important application of solid–liquid mixing is the preparation of brine from sodium formate. This material has been widely used as a drilling and completion fluid in challenging environments such as the Barents Sea. In this paper, large-eddy simulations of a turbulent flow in a solid–liquid baffled cylindrical mixing vessel with large number of solid particles are performed to obtain insight into the fundamental aspects of a mixing tank. The impeller-induced flow at the blade tip radius is modeled by using the dynamic-mesh Lagrangian method. The simulations are four-way coupled, which implies that both solid–liquid and solid–solid interactions are taken into account. By employing a soft particle approach the normal and tangential forces are calculated acting on a particle due to viscoelastic contacts with other neighboring particles. The results show that the granulated form of sodium formate may provide a mixture that allows faster and easier preparation of formate brine in a mixing tank. In addition it is found that exceeding a critical size for grains phenomena, such as caking, can be prevented. The obtained numerical results suggest that by choosing appropriate parameters a mixture can be produced that remains free-flowing no matter how long it is stored before use.     

微通道液体流动双电层阻力效应

采用数值方法求解双电层的Poisson-Boltzmann方程和液体运动的Navier-Stokes方程,研究微通道双电层对压强梯度液体流动的阻力效应． 量纲分析表明,双电层阻力大小可以用一个无量纲的电阻力数表示．它与液体的介电系数、固体表面的zeta电位平方成正比,与液体的动力粘性系数、电导率以及微通道的宽度平方成反比．在计算流动诱导的流动电位势和电阻力时,提出电流密度平衡条件,可以消除传统电流平衡条件导致的固壁附近产生局部回流的不合理物理现象．还给出不同电阻力数的微通道流量、流量损失率、速度剖面的数值结果,合理解释了双电层对微通道液体流动的阻力效应．     

Three‐dimensional solidification with two possible crystallization states: Existence of solutions with flow in the melt

In this paper we discuss the existence of solutions of a system of nonlinear and singular partial differential equations constituting a phase field model with convection for non‐isothermal solidification/melting of certain metallic alloys in the case where two different kinds of crystallization are possible. Each one of these crystallization states is described by its own phase field, while the liquid phase is described by another one. The model also allows the occurrence of fluid flow in non‐solid regions, which are a priori unknown, and then we have a free‐boundary value problem. Thus, the model relates the evolutions of these three phase fields, the temperature of the solidification/melting process and the fluid flow in non‐solid regions. Copyright © 2009 John Wiley & Sons, Ltd.     

Rheological effect on thermocapillary flow of a liquid film jet painted on a moving boundary

In the present paper, a liquid (or melt) film of relatively high temperature ejected from a vessel and painted on the moving solid film is analyzed by using the second-order fluid model of the non-Newtonian fluid. The thermocapillary flow driven by the temperature gradient on the free surface of a Newtonian liquid film was discussed before. The effect of rheological fluid on thermocapillary flow is considered in the present paper. The analysis is based on the approximations of lubrication theory and perturbation theory. The equation of liquid height and the process of thermal hydrodynamics of the non-Newtonian liquid film are obtained, and the case of weak effect of the rheological fluid is solved in detail.     

Flow through a porous medium with mass removal and diffusion

A one-dimensional model of filtration through a saturated porous medium with a mutual action between the solid matrix and the flow is investigated. The substances removed from the porous soil are both particles transported by the liquid flow and substances which diffuse in the fluid. Received June 30, 1997     

Numerical simulation of immersion quenching process of an engine cylinder head

In this article, we present the numerical simulations of a real cylinder head quench cooling process employing a newly developed boiling phase change model using the commercial CFD code AVL-FIRE v8.5. Separate computational domains constructed for the solid and liquid regions are numerically coupled at the interface of the solid–liquid boundaries using the AVL-Code-Coupling-Interface (ACCI) feature. The boiling phase change process triggered by the dipping hot metal and the ensuing two-phase flow is handled using an Eulerian two-fluid method. Multitude of flow features such as vapor pocket generation, bubble clustering and their disposition, are captured very effectively during the computation, in addition to the variation of the temperature pattern within the solid region. A comparison of the registered temperature readings at different monitoring locations with the numerical results generates an overall very good agreement and indicates the presence of intense non-uniformity in the temperature distribution within the solid. Overall, the predictive capability of the new boiling model is well demonstrated for real-time quenching applications.