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1.
非牛顿流体入口收敛流动分析   总被引:5,自引:0,他引:5  
梁基照 《力学学报》1990,22(1):79-85
本文讨论了非牛顿流体的入口收敛流动问题,考虑到粘弹性流体在流动中的粘滑行为,应用最小能原理,导出了扩展的入口收敛流边界流线方程和流体自然收敛锥角方程,并与前人的工作进行了比较和分析。  相似文献   

2.
单裂缝中携砂液流动规律研究   总被引:3,自引:0,他引:3  
裂缝中携砂液流动是一种固液两相流,携砂液的运移与支撑剂的铺置是水力压裂裂缝保持导流能力的关键.本文基于FLUENT流体计算软件,采用双流体模型,将颗粒看作拟流体,携砂液按照牛顿流体处理,分析了支撑剂体积分数α_s、阿基米德数Ar、颗粒雷诺数Re以及裂缝入口边界对流动规律的影响.研究结果表明:携砂液在裂缝中的流动过程中,发展成为支撑剂体积分数不同的四个区域,包括砂堤区、颗粒悬浮区、颗粒滚流区和无砂区;支撑剂的沉降程度随着支撑剂体积分数和阿基米德数的增加而增加,而随着雷诺数增加而降低;入口为网眼型时,进入裂缝后过流面积的增加导致流速突降,使得支撑剂更容易在入口处产生堆积,在同一入口流速下,较均匀入口的工况铺砂高度大.  相似文献   

3.
采用模拟黏弹流体挤出胀大的方法,计算了IUPAC-LDPE熔体经过4:1轴对称收缩流道的流动.计算的相对涡强度、入口校正和献中的结果基本一致,给出的流场也显示出计算结果是合理的.表明该方法能够适用于用积分型PSM模型表征的黏弹流体在收缩流道内的流动模拟.  相似文献   

4.
水平井变质量流研究进展   总被引:15,自引:0,他引:15  
综述了水平井筒沿管壁具有流体流入的变质量流动的最新研究 进展.内容包括:考虑油藏流体流入时井筒流动压力及产量的计算,具 有不同流入时管壁摩擦系数的经验计算公式,以及流体径向流入井筒 后流动阻力损失产生的机理分析等.重点介绍了水平井筒变质量流动 阻力系数的计算,同时文中还介绍了井筒两相变质量流动损失产生的 机理和数值模拟研究进展.  相似文献   

5.
采用大涡模拟方法和单方程亚格子模式对小尺度量进行模拟。研究了不同强度壁面射流激励对圆管内气相流动的影响,模拟结果给出了射流对瞬态拟序结构发展、时平均流向速度分布的影响。随着射流强度的增加,射流入口附近流体的回流现象增强。射流强度足够大时可以减小管壁处的切应力值,同时会减小壁面附近流动速度,这种速度分布会导致气体夹带颗粒的能力下降,从而在实际两相流动中容易造成壁面附近的气粒返混现象。  相似文献   

6.
为了研究节水水嘴起泡器内部两相流的流动规律,采用Fluent软件对其内部流场进行数值模拟.根据起泡器内部流场的流动特性,采用欧拉两相流模型以及RNG(re—normalization group)κ-ε湍流模型,分析起泡器出口截面气液两相体积分数和速度的分布特点.结果表明:增大入口水流速度可以加快分散出口截面气液两相的分布,缩短流体流动的稳定时间;整流网具有分散流体,降低流速的作用;错开整流网相邻层之间的网格可以改善出口截面的液相分布;本模型中整流网采用三层网格达到较好的出水效果.  相似文献   

7.
微通道不仅仅是作为流体流动的单元, 更是进行流体控制的工具, 微通道自身特性和特征用在实现微流体的驱动、进样、混合、分离以及液滴的产生、控制等方面已经表现出了良好的效果. 由于微通道中比表面积非常大, 表面效应极大影响流体流动, 近年来多数研究集中在应用表面效应来实现微流体驱动与控制, 而以利用微通道结构特征实现流体流动控制为目标的研究成果相对较少. 为了提高对通道构型作用的认识, 主要介绍了基于微通道构型的无可动部件的流体微阀和基于微通道构型微小液滴的产生及流动控制器两个方面的发展情况, 表明微通道构型在微流体控制中同样可以发挥重要作用, 甚至有望带来微流控技术的突破.  相似文献   

8.
机匣与叶片的相对转动是影响涡轮叶顶间隙流动的重要冈素之一.对LISA 1.5级轴流涡轮间隙内部流动的数值计算结果表明:叶片转动对涡轮间隙流动有阻塞作用.叶片静止时,由于阻塞作用消失,导致间隙入口速度增大,间隙流鼍增加,并且通过间隙的流体全部卷起形成间隙涡.同时在叶片顶部吸力面侧前缘、中部各形成一个间隙涡,使得间隙流动损失增加.而且转速下降会加剧动叶出口截面气流过偏/偏转不足现象.同时叶片静止时,间隙前部各个弦长截面内静压自间隙入口开始一直呈增加趋势,直到叶片尾缘附近截面,间隙截面内静压才逐渐稳定.  相似文献   

9.
本文研究了非牛顿流体在Hele-Shaw模型中的流动特性,并用摄动法求出了Bingham流体、Power-law流体的速度分布、压力降与流量的关系,分析了屈服应力及幂律指数对物理参数的影响.  相似文献   

10.
黏弹性流体纯弹性不稳定现象研究综述   总被引:1,自引:0,他引:1  
近年来黏弹性流体流动的纯弹性不稳定现象引起了越来越多学者的关注与研究,与牛顿流体惯性不稳定现象不同,这种现象是由黏弹性流体流动中的弹性应力和黏性力之间相互作用,使得在较低的雷诺数Re下即可产生复杂的流动分岔不稳定现象.当流动中的弹性数较大时,在ReRec(惯性不稳定性产生的临界雷诺数)下,黏弹性流体流动中也可能产生完全由弹性应力引起的纯弹性不稳定现象.以Taylor–Couette流动为基础,对黏弹性流体流动中产生纯弹性不稳定现象的研究现状从实验、理论分析和数值模拟3个方面进行总结.通过对比这3个方面,总结了弹性流动不稳定现象发生的过程与机理、流动不稳定性产生的影响因素及其作用方式,并对目前研究的不足之处以及今后可能的发展趋势作了分析和展望.  相似文献   

11.
The influence of the upper wall on the die entry flow of viscoeleastic fluids was investigated experimentally. Aqueous solutions of Separan AP-30 were pushed out by a compressed gas pressure through a capillary attached to the bottom of a reservoir having a height-adjustable upper wall. The driving gas pressure, the flow rate and the pressure at the center of the upper wall were measured and the flow patterns in the entry region above the inlet section of the capillary were observed. Flow rate measurements under the condition of constant driving pressure reveal that the maximum height of the upper wall required to reduce the flow rate is much larger for viscoelastic fluids than for Newtonians, and that this effect of the upper wall becomes more conspicuous with increasing driving pressure. What is curious is that under some conditions the flow rate is larger for a moderate upper wall height than for an infinite. These phenomena are shown to be attributed to the increasing and the reducing effects of the entry pressure loss by the upper wall. The latter effect may be called a new type of pressure-loss reduction phenomenon of viscoelastic fluids. The observation of the flow and the measurement of the pressure at the upper wall center show that typical flow patterns of the die entry flow of viscoelastic fluids are responsible for the far greater pressure loss than for Newtonians, and that the entry pressure loss for a spiralling flow is a little smaller than for the other two types even at an equal driving pressure.  相似文献   

12.
The problem of viscoelastic fluid flow in a convergent-divergent channel is considered. A mathematical model and the results of numerical investigations are presented. A model of the differential type is used to describe the rheological properties of viscoelastic fluids. A comparative analysis of the flow parameters of generalized Newtonian and viscoelastic fluids in the channels considered is carried out on the basis of the results of numerical calculations.  相似文献   

13.
A low cost, low power laser-speckle photographic technique has been developed and is duscussed for the measurement of point velocities in slow laminar flows. The technique is particularly suitable for axisymmetric flows where the two velocity components can be easily measured. The accuracy of the technique is established by measurement of the velocity distribution for Poiseuille flow and from data obtained for acceleration of an inelastic Newtonian fluid through a four-to-one circular contraction. Preliminary results are also presented in the contracting flow field for a non shear-thinning highly elastic fluid. These data are particularly significant for verification of finite element numerical solutions currently being developed for viscoelastic fluids in circular entry flows.  相似文献   

14.
This paper presents a mathematical model for describing approximately the viscoelastic effects in non-Newtonian steady flows through a porous medium. The rheological behaviour of power law fluids is considered in the Maxwell model of elastic behaviour of the fluids. The equations governing the steady flow through porous media are derived and an analytical solution of these equations in the case of a simple flow system is obtained. The conditions for which the viscoelastic effects may become observable from the pressure distribution measurements are shown and expressed in terms of some dimensionless groups. These have been found to be relevant in the evaluation of viscoelastic effects in the steady flow through porous media.  相似文献   

15.
An associative polymer–surfactant system has been used to observe the effects of chain conformation in the entry flow through a microfabricated planar 16:1:16 contraction–expansion geometry. The well-studied system of the flexible polymer poly(ethylene oxide) (PEO) and anionic surfactant sodium dodecyl sulfate (SDS) was used. Dilute polymer solutions with increasing SDS concentration were characterized in steady and dynamic shear, as well as capillary breakup extensional rheology. Based on this characterization, the primary quantitative difference is an increase in zero-shear viscosity as a result of the PEO chain expansion brought on by association of SDS surfactant micelles. However, these quantitatively similar solutions were observed to exhibit much more qualitatively different flow patterns via fluorescent streak imaging in the entry flow. In contrast to previous work on PEO solutions, the PEO–SDS systems were observed to transition to a steady viscoelastic flow regime characterized by stable lip vortices at much lower elasticity and Weissenberg numbers. The resulting insight gained regarding the utility of microfluidic flows in elucidating effects of subtle conformational changes further illustrates the potential for using microfabricated devices as rheometric tools for measuring the properties of dilute and weakly viscoelastic fluids.  相似文献   

16.
The phenomena of flow reduction and flow enhancement was observed in case of viscoelastic and viscoinelastic fluids flowing through packed beds, respectively. In this study, the pressure drop-flow rate behaviors for the flow of Newtonian (water), non-Newtonian viscoinelastic (Carboxy methyl cellulose solution in water, CMC) and viscoelastic (Polyacrylamide solution in water, PAA) fluids have been experimentally studied and pressure drop behavior compared with existing models for viscoinelastic and viscoelastic fluids. Based on the observed data, an appropriate empirical correlation for pressure drop prediction in case of non-Newtonian fluid flowing through packed bed has been proposed. The correlation predicts the data well to within a reasonable accuracy.  相似文献   

17.
康建宏  谭文长 《力学学报》2018,50(6):1436-1457
基于修正的Darcy模型, 介绍了多孔介质内黏弹性流体热对流稳定性研究的现状和主要进展. 通过线性稳定性理论, 分析计算多孔介质几何形状(水平多孔介质层、多孔圆柱以及多孔方腔)、热边界条件(底部等温加热、底部等热流加热、底部对流换热以及顶部自由开口边界)、黏弹性流体的流动模型(Darcy-Jeffrey, Darcy-Brinkman-Oldroyd以及Darcy-Brinkman -Maxwell模型)、局部热非平衡效应以及旋转效应对黏弹性流体热对流失稳的临界Rayleigh数的影响. 利用弱非线性分析方法, 揭示失稳临界点附近热对流流动的分叉情况, 以及失稳临界点附近黏弹性流体换热Nusselt数的解析表达式. 采用数值模拟方法, 研究高Rayleigh数下黏弹性流体换热Nusselt数和流场的演化规律,分析各参数对黏弹性流体热对流失稳和对流换热速率的影响.主要结果:(1)流体的黏弹性能够促进振荡对流的发生;(2)旋转效应、流体与多孔介质间的传热能够抑制黏弹性流体的热对流失稳;(3)在临界Rayleigh数附近,静态对流分叉解是超临界稳定的, 而振荡对流分叉可能是超临界或者亚临界的,主要取决于流体的黏弹性参数、Prandtl数以及Darcy数;(4)随着Rayleigh数的增加,热对流的流场从单个涡胞逐渐演化为多个不规则单元涡胞, 最后发展为混沌状态.   相似文献   

18.
The planar contraction flow is a benchmark problem for the numerical investigation of viscoelastic flow. The mathematical model of three‐dimensional viscoelastic fluids flow is established and the numerical simulation of its planar contraction flow is conducted by using the penalty finite element method with a differential Phan‐Thien–Tanner constitutive model. The discrete elastic viscous split stress formulation in cooperating with the inconsistent streamline upwind scheme is employed to improve the computation stability. The distributions of velocity and stress obtained by simulation are compared with that of Quinzani's experimental results detected by laser–doppler velocimetry and flow‐induced birefringence technologies. It shows that the numerical results agree well with the experimental results. The numerical methods proposed in the study can be well used to predict complex flow patterns of viscoelastic fluids. Copyright © 2009 John Wiley & Sons, Ltd.  相似文献   

19.
The problem of the stability of the flow of viscoelastic fluids has fundamental importance for the technology of the production of polymer products and viscosimetry. This problem is not reduced only to classical inertial turbulence. A number of other mechanisms leading to flow instability are known [1, 2]. A thermal mechanism based on the allowance for dissipative heating and elastic properties within the framework of a linear model of a viscoelastic fluid was drawn upon to explain this phenomenon in [1]. The possibility of a self-oscillatory mode of flow was demonstrated on the basis of a qualitative analysis of the theological equation and the equation of heat balance in application to simple shear flow and uniform stretching. A theoretical analysis of the self-heating of flowing systems possessing viscoelastic properties is carried out in the present report. The main laws of the thermal instability of viscoelastic fluids discovered in [1] are described.Translated from Zhurnal Prikladnoi Mekhaniki i Tekhnicheskoi Fiziki, No. 3, pp. 115–122, May–June, 1979.  相似文献   

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