Computer Simulation of the Flow of Non-Newtonian Two-Phase media in Areas of Complex Geometry

IF 0.7 4区 工程技术 Q4 ENGINEERING, CHEMICAL
R. I. Ibyatov, F. G. Akhmadiev, R. A. Galimov, D. M. Galiev
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引用次数: 0

Abstract

Computer modeling of the flow of two-phase non-Newtonian media in areas of complex geometry, which often applies to the elements of various technological equipment, is considered. The basis of the computer modeling is a mathematical model of the flow of non-Newtonian two-phase media in channels and pipes with various curved walls. To construct a mathematical model of the flow of non-Newtonian two-phase media, the equations of conservation of mass and momentum of the mechanics of heterogeneous media are used with the corresponding closing relations for the force of interphase interaction and the rheological law of the state of the medium. Simplified equations taking into account flow features close to one-dimensional, written in an orthogonal coordinate system associated with the flow area, are solved numerically using a modified method of equal flow surfaces. An algorithm for numerical flow calculations is constructed for computer simulation of the process. In the numerical calculations, the location and number of surfaces of equal flow rates varies in a wide range, taking into account the characteristics of the flow, and reasonable input (initial) values of the longitudinal velocity on the streamlines are specified. Numerical calculations are carried out for areas of parabolic and conical shapes, taking into account the inlet section of the flow and the influence of the centrifugal force field. A computational experiment is performed for various values of the channel parameters, the rheological law of the state of the medium, and the flow regimes of the two-phase medium. As a result, it is found that in the initial section the flow is transformed from an initial flat profile to a parabolic one. The flow velocities slow down near the channel walls and accelerate in the center of the flow region. Because of this, in the initial section of the flow region, the streamlines are bent. Knowledge of the velocity field of the carrier phase makes it possible to determine the trajectories of motion of the dispersed phase, which is a determining factor for many technological processes. The constructed mathematical model that describes the hydrodynamic situation in the flow region allows us to conduct a computational experiment to calculate the flow of two-phase non-Newtonian media in curved channels and pipes of complex geometry using the modified method of equal flow surfaces. In this case, specific shapes of the flow region are specified by specifying the corresponding Lame coefficients for the flow region. Based on computer modeling, various flow regimes and the influence of various geometric characteristics of the channel, mass forces, and parameters of the rheological law of the state of the medium on the hydrodynamic flow conditions are studied. At different values of the nonlinearity parameters in the power law of state, the centrifugal force, with its increase, has a stronger influence on the hydrodynamic situation in the channel. The results of computer modeling make it possible to pose and solve problems of optimal hardware design of the corresponding technological processes.

Abstract Image

非牛顿两相介质在复杂几何区域流动的计算机模拟
考虑了复杂几何区域中两相非牛顿介质流动的计算机建模,这通常适用于各种工艺设备的元件。计算机模拟的基础是非牛顿两相介质在具有不同弯曲壁的通道和管道中流动的数学模型。为了建立非牛顿两相介质流动的数学模型,采用了非牛顿两相介质力学的质量守恒方程和动量守恒方程以及相间相互作用力和介质状态流变定律的对应关系。采用改进的等流面法,在与流动面积相关的正交坐标系中,对考虑接近一维流动特征的简化方程进行了数值求解。建立了一种数值流场计算算法,对该过程进行了计算机模拟。在数值计算中,考虑到流动的特性,等流量曲面的位置和数量在很大范围内变化,并规定了流线上纵向速度的合理输入(初始)值。在考虑气流入口截面和离心力场影响的情况下,对抛物线形和锥形区域进行了数值计算。对不同的通道参数值、介质状态的流变规律和两相介质的流态进行了计算实验。结果发现,在初始截面,流动由初始的平坦型转变为抛物线型。流动速度在通道壁面附近减慢,在流动区域中心加速。因此,在流区的初始部分,流线是弯曲的。对载相速度场的了解使确定分散相的运动轨迹成为可能,这是许多工艺过程的决定因素。建立了描述流区水动力情况的数学模型,使我们能够利用改进的等流面法进行两相非牛顿介质在弯曲通道和复杂几何形状管道中的流动计算实验。在这种情况下,通过指定流区的相应Lame系数来指定流区的特定形状。在计算机模拟的基础上,研究了各种流动状态以及各种通道几何特性、质量力和介质状态流变规律参数对流体动力流动条件的影响。在状态幂律非线性参数取值不同时,离心力对通道内水动力状况的影响随着离心力的增大而增强。计算机建模的结果为提出和解决相应工艺流程的硬件优化设计问题提供了可能。
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来源期刊
CiteScore
1.20
自引率
25.00%
发文量
70
审稿时长
24 months
期刊介绍: Theoretical Foundations of Chemical Engineering is a comprehensive journal covering all aspects of theoretical and applied research in chemical engineering, including transport phenomena; surface phenomena; processes of mixture separation; theory and methods of chemical reactor design; combined processes and multifunctional reactors; hydromechanic, thermal, diffusion, and chemical processes and apparatus, membrane processes and reactors; biotechnology; dispersed systems; nanotechnologies; process intensification; information modeling and analysis; energy- and resource-saving processes; environmentally clean processes and technologies.
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