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1.
考虑宾汉流体本构关系的特点,建立了适用于宾汉流体的修正动量方程和Kτ-ετ模型方程。采用压力耦合半隐式SIMPLE算法,通过流场的数值计算研究,指出了宾汉流体本身的物性参数(如屈服应力、塑性粘度)对其湍流强度有着重要影响。  相似文献   

2.
离心泵是流体力学理论最为典型的应用,很多流体力学教材都将离心泵列为重要章节。离心泵输送单一介质时内部流体是圆周运动和相对运动的复合运动,输送固液两相时还会存在两相速度差,可见其内部流动非常复杂。如果将这些复杂的流体运动可视化,让学生看到这种流动现象,将会成为理论教学非常好的补充,加强学生对课堂知识的理解和巩固。为了将内部流动更好地呈现出来,本实验台将离心泵透明可视化,再做了局部改造后,叶轮和蜗壳区域可全部无遮挡地展现出来,再利用粒子图像测速技术捕捉内部流动,在宏观方面来讲,可开展单一介质或者两相介质在叶轮中的流动情况的观察实验,在微观方面来讲,可开展观察单一介质速度场和两相介质相对速度的测量实验。  相似文献   

3.
在Fluent软件中应用RNG $k$-$\varepsilon$湍流模型及流体体积函数(VOF)对座便 器内部三维湍流流动进行了雷诺平均N-S方程的数值模拟,得到 了座便器内流场三维流动形态,研究了座便器虹吸管内流动规律,分析了虹吸管形状对流速 分布、压力分布及虹吸性能的影响,以三维湍流场的分析结果为依据,实现了座便器虹吸管 道的优化设计. 通过PIV测试数据验证了三维湍流数值模拟结果的准确性.  相似文献   

4.
吴先鸿  陈矛章 《力学学报》1998,30(3):257-266
发展了一种研究叶轮机内动、静叶间的相互作用的新方法———扰动涡方法,它利用全三维的定常解为基础解,并由此给出非定常扰动场的初始解.为计算叶片对扰动场的响应过程,采用拉格朗日方法追踪扰动涡团的对流流动过程,用确定性涡方法来描述流体的粘性扩散过程.发展了代数湍流模型(Baldwin Lomax湍流模型)在尾迹中的应用方法,克服了其它数值方法中无法准确捕捉尾迹中心线的运动轨迹,以及计算出的边界层外的湍流涡粘性系数偏大的缺陷.利用该方法计算轴流叶轮机内由于动、静叶间的相互作用而引起的非定常流动过程,与实验的对照表明,模拟结果与实验数据吻合得相当好,从而说明本文发展的方法是可信的,为更直观地描述尾迹等非定常因素的流动及叶轮机内的掺混问题提供依据.  相似文献   

5.
利用作者建立的描述密相液固两相湍流的 KET模型和推导的基本控制方程组 ,在处理壁面边界条件时考虑了颗粒和叶片的相互碰撞作用 ,对离心泵叶轮内密相液固两相流动进行了数值模拟 ,得到了泵叶轮内两相流动的一些规律 ,为液固两相流泵的设计提供了一定的理论依据。  相似文献   

6.
搅拌槽流场的实验研究   总被引:4,自引:0,他引:4  
李玉麟  毛德明 《实验力学》1996,11(3):285-292
利用二维激光多普勒测速仪在内径为250mm的搅拌槽内对DT叶轮和PT叶轮进行了流场测试,获得了不同几何参数的叶轮在不同工况下的二维时均速度场和湍流强度、雷诺应力、剪切速率分布。为进一步研究搅拌器的流动特性,开发新型搅拌叶轮提供了可靠的实验依据。  相似文献   

7.
大速差射流预燃室内三维回流两相湍流的数值模拟   总被引:1,自引:0,他引:1  
本文由多流体两相流模型、气相湍流κ-ε模型和颗粒湍流代数模型出发,成功地模拟了真实形状大速差射流预燃室中三维湍流回流两相流动,得到了这类复杂的气固两相流中不同纵横截面上气相速度场、颗粒速度场及浓度场和两相湍流度场的分布,并且获得了与实验定性一致的合理结果,揭示了预燃室中气固两相流动与混合的主要物理特征,探讨了大速差射流技术稳焰和强化燃烧的两相流动机理。  相似文献   

8.
大速差射流预燃室内三维回流两相湍流的数值模拟   总被引:2,自引:0,他引:2  
本文由多流体两相流模型、气相湍流κ-ε模型和颗粒湍流代数模型出发,成功地模拟了真实形状大速差射流预燃室中三维湍流回流两相流动,得到了这类复杂的气固两相流中不同纵横截面上气相速度场、颗粒速度场及浓度场和两相湍流度场的分布,并且获得了与实验定性一致的合理结果,揭示了预燃室中气固两相流动与混合的主要物理特征,探讨了大速差射流技术稳焰和强化燃烧的两相流动机理。  相似文献   

9.
本文提出一种求解离心式叶轮流场的数值方法,将流动求解区域离散为有限个由流线构成其边界的单元,采用伽辽金法建立的单元方程在一条流束上集合为方程组,流线上的节点坐标亦作为未知量包含在有限元方程中,通过扫描计算,逐步解得流线位置及流动参数。本文应用叶轮的通流理论流动模型,采用扫描流速有限元方法对离心泵叶轮流场进行了计算,并与有关文献作了比较。  相似文献   

10.
在不同进口导叶预旋角度下,采用非定常的方法对进口导叶/叶轮/扩压器三部件之间非定常相干进行了数值与实验研究,探讨了三部件之间动静相干的机理.结果表明,在进口导叶/叶轮/扩压器三部件相干时,最大的脉动压力出现在叶轮和扩压器之间的动静交界面上.当进口导叶预旋角度存在时,叶轮与扩压器之间无叶区内的非定常流动以叶轮叶片通过频率和1/2叶片通过频率为基频;而当扩压器进口安装角增大时,径向间隙内的流动则主要以1/2叶片通过频率为基频.在不同的配置下,湍流强度和非定常度均有朝向轮盘增加的趋势.在进口导叶正预旋60°同扩压器进口安装角为17°时的配置有增大湍流强度和非定常度的趋势.  相似文献   

11.
I.IntroductionBinghamfluidisonebranchofnon-Newtonianfluid,suchascrudeparaffinoil,highsediment--ladenwaterflow,highconcentrationmudandthelikewhicharetransportedinpipelinesinmanyindustries,soit'sofgreatsignificancetostudytheflowmechanismsofBinghamfluid.Tsaietal.II]studiedthelinkagebetweenBinghamfluidandpluggedflow.Wangetal.I2]measuredtheturbulencestructureofBinghammud.Mengetal.[3]researchedthekineticenergycorrectionfactorofBinghamfluidinacircularpipe.However,thestudyofBinghamfluidsofarisn't…  相似文献   

12.
ANALYTICALSOLUTIONSOFTHEHELICALFLOWOFNONNEWTONIANFLUIDINECCENTRICANNULARSPACEZhangHai-qiao(张海桥)WuJi-zhou(吴继周)(TheDepartmentof...  相似文献   

13.
In the present paper the flow of a Bingham fluid between two parallel porous walls is studied. One of the walls moves with constant velocity parallel to the other, which is fixed, while a longitudinal pressure gradient exists, as well as a transverse flow field due the porosity of the walls. An exact analytical solution is given for the u-velocity field, which has four different forms depending on the values of the three dimensionless parameters, which are the Bingham, Couette and Reynolds numbers.  相似文献   

14.
Flow of Bingham plastics through straight, long tubes is studied by means of a versatile analytical method that allows extending the study to a large range of tube geometries. The equation of motion is solved for general non-circular cross-sections obtained via a continuous and one-to-one mapping called the shape factor method. In particular the velocity field and associated plug and stagnant zones in tubes with equilateral triangular and square cross-section are explored. Shear stress normal to equal velocity lines, energy dissipation distribution and rate of flow are determined. Shear-thinning and shear-thickening effects on the flow, which cannot be accounted for with the Bingham model, are investigated using the Hershey-Bulkley constitutive formulation an extension of the Bingham model. The existence and the extent of undeformed regions in the flow field in a tube with equilateral triangular cross-section are predicted in the presence of shear-thinning and shear-thickening as a specific example. The mathematical flexibility of the analytical method allows the formulation of general results related to viscoplastic fluid flow with implications related to the design and optimization of physical systems for viscoplastic material transport and processing.  相似文献   

15.
张准  朱克勤 《力学学报》2003,35(2):135-139
基于油膜内屈服面位置可能出现的4种情况,Tichy提出了用于Bingham流体滑动轴承特性及其屈服面位置的计算方法,在将该计算方法推广到电流变液滑动轴承的计算时,发现随着外加电场强度的变形,出现了轴承风屈服面位置不变的非物理结果,而且Tichy的方法只能适用于无限宽滑动轴承,为了对有限宽度的电流变液滑动轴承进行数值研究,采用了类Bingham模型,通过差分离散和超松驰迭代的方法对雷诺方程进行求解,计算结果表明:电流变流滑动轴承内的压力分布可以通过外加电场强度来控制,轴承间隙内屈服面位置随电场强度变化而产生的移动是使轴承润滑性能得以改变的重要力学机制;在轴承以高剪切速率运转时,由于电流变液表观黏度随电场强度的变化已经很小,该机制在轴承的设计中尤为重要。  相似文献   

16.
The flow induced by a sphere rotating inside a non-Newtonian, Bingham fluid has been investigated numerically. The rotating sphere is enclosed in a concentric cubic box with solid boundaries. The Bingham number varied between 0.01 and 100,000 and the Reynolds number varied between 0.01 and 10,000. The torque increases with the Bingham number and reaches an asymptotic state at large Bn. The torque is independent of the Reynolds number at high Bn. The yielded region around the sphere has been determined and an empirical equation is found for its extent.  相似文献   

17.
范椿  陈耀松 《力学学报》1995,27(Z1):14-19
导出了描述Bingham流体在旋转圆盘上流动的基本方程,用差分方法数值解薄膜厚度分布方程,得到二种类型的厚度分布。数值解分别和计算机磁盘的厚度分布,Jenekhe等的实验结果定性一致。  相似文献   

18.
The equations for the nonhomogeneous incompressible Herschel–Bulkley fluid are considered and existence of a weak solution is proved for a boundary-value problem which describes three-dimensional flows between two eccentric cylinders when in each two-dimensional cross-section annulus the flow characteristics are the same. The rheology of such a fluid is defined by a yield stress τ* and a discontinuous stress-strain law. A fluid volume stiffens if its local stresses do not exceed τ*, and a fluid behaves like a nonlinear fluid otherwise. The flow equations are formulated in the stress–velocity–density–pressure setting. Our approach is different from that of Duvaut–Lions developed for the classical Bingham viscoplastic fluids. We do not apply the variational inequality but make use of an approximation of the generalized Bingham fluid by a non-Newtonian fluid with a continuous constitutive law.  相似文献   

19.
A mathematical study is developed for the electro-osmotic flow of a nonNewtonian fluid in a wavy microchannel in which a Bingham viscoplastic fluid model is considered. For electric potential distributions, a Poisson-Boltzmann equation is employed in the presence of an electrical double layer(EDL). The analytical solutions of dimensionless boundary value problems are obtained with the Debye-Huckel theory, the lubrication theory, and the long wavelength approximations. The effects of the Debyelength parameter, the plug flow width, the Helmholtz-Smoluchowski velocity, and the Joule heating on the normalized temperature, the velocity, the pressure gradient, the volumetric flow rate, and the Nusselt number for heat transfer are evaluated in detail using graphs. The analysis provides important findings regarding heat transfer in electroosmotic flows through a wavy microchannel.  相似文献   

20.
In the present study we propose a new version of the lattice-Boltzmann (LB) method for the simulation of flow of yield-stress liquids. Unlike traditional LB methods, collisions are treated implicitly, i.e., the collision term is chosen in such a way that the stress and strain rate tensors satisfy the constitutive equation after the collision. This approach requires the solution of a (one-dimensional) non-linear algebraic equation at each point and at each time step. In the practically important cases of a Bingham liquid this equation can be solved analytically. We calculated the flow of Bingham fluid through a channel and periodic mesh of cylinders.  相似文献   

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