多相流水力学现象方程的推导

IF 0.3 Q4 ENGINEERING, PETROLEUM Nafta-Gaz Pub Date : 2023-11-01 DOI:10.18668/ng.2023.11.06
Gasim A. Mamedov, Rauf Kh. Melikov, Natig M. Abbasov, M. S. Rahimova
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A function, denoted as φi (x, y, z, t), has been introduced, which indicates the probability of the presence of the i-th phase in the vicinity of a given point in space at time t, or that the given point of space x, y, z at time t belongs to the set of points of the i-th phase. On the other hand, this probability can be interpreted as the volumetric concentration of the i-th phase at a given point in space (i.e., the ratio of the measure of the set of points belonging to the i-th phase in the vicinity of the point under consideration at time t to the measure of the entire set of points in the surrounding area). This hypothetical medium, being equivalent to the original one, serves as a model for a multi-phase (inhomogeneous, heterogeneous, two-phase) medium. The uniqueness of the model arises from its construction. 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引用次数: 0

摘要

在文章中,多相(非均相、异相)介质被视为一个宏观系统(连续体),由若干相(至少两相)组成,例如载体相(液体、蒸汽或气体)和承载相(固体颗粒、气泡或液滴)。由于新质量的加入或分离,这些相的质量和混合物会随时间发生连续变化。该模型考虑到了相间转换、混合物内部的不连续性,以及各相根据其位置成为连续或离散相的可能性。利用离散相在空间中的位置、形状和大小都是随机的这一事实,开发了一种初步平滑不连续性的方法。我们引入了一个函数φi (x, y, z, t),表示第 i 个相位在时间 t 空间给定点附近出现的概率,或时间 t 空间 x、y、z 给定点属于第 i 个相位点集合的概率。另一方面,这种概率也可以解释为第 i 相在空间给定点上的体积浓度(即在时间 t 时,在所考虑的点附近属于第 i 相的点集的测量值与周围区域整个点集的测量值之比)。这种假设介质等同于原始介质,可作为多相(非均质、异相、两相)介质的模型。模型的唯一性源于其构造。此外,本文还探讨了有关连续介质的多相(两相悬浮液携带)流体力学的几个主要理论和实验研究领域。本文还讨论了现有研究中取得的最重要成果。对多相(两相)系统运动数学描述的已知理论和湍流流体力学特征的平均方法进行了批判性分析。在半经验湍流理论的框架内,对现有著作中提出的多相流流体力学方程组进行了闭合。在自然界中,绝大多数多相(两相、不均匀)混合物都表现出湍流行为,因此对其进行研究是一项重要的实际任务。湍流多相流运动的数学描述依赖于定型的力学定律。对于多相(两相)流运动的数学描述,不同研究人员在不同时期提出的运算分析方法具有不同程度的近似性和某些有限的应用领域。为湍流多相(两相、携带悬浮物)流的运动制定微分方程的主要挑战之一是,在混合物的湍流中,流动特性随时间随机发生混沌变化,在空间的每一点上,无论在大小还是方向上,都存在着具有弱不连续性和强不连续性的表面。因此,严格来说,多相流的实际速度和压力值不能被视为混合物所占整个区域的空间和时间坐标的连续函数。
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Derivation of phenomenological equations of hydromechanics of multi-phase flows
In the article, a multi-phase (non-homogeneous, heterogeneous) medium is considered as a macrosystem (continuum) composed of several (at least two) phases, such as a carrier phase (liquid, vapor or gas) and a carried phase (solid particles, bubbles or drops).The masses and mixtures of these phases undergo continuous changes over time due to the addition or separation of new masses to or from both phases. The model takes into account interphase transitions, discontinuities inside the mixture, and the possibility of phases being either continuous or discrete, depending on their location. A method for preliminary smoothing of discontinuities has been developed, leveraging the fact that the location in space, as well as the shape and size of the discrete phase are random. A function, denoted as φi (x, y, z, t), has been introduced, which indicates the probability of the presence of the i-th phase in the vicinity of a given point in space at time t, or that the given point of space x, y, z at time t belongs to the set of points of the i-th phase. On the other hand, this probability can be interpreted as the volumetric concentration of the i-th phase at a given point in space (i.e., the ratio of the measure of the set of points belonging to the i-th phase in the vicinity of the point under consideration at time t to the measure of the entire set of points in the surrounding area). This hypothetical medium, being equivalent to the original one, serves as a model for a multi-phase (inhomogeneous, heterogeneous, two-phase) medium. The uniqueness of the model arises from its construction. In addition, this paper considers several main areas of theoretical and experimental research concerning the hydrodynamics of a multi-phase (two-phase suspension-carrying) flow of a continuous medium. It also discusses the most important results achieved in existing works. A critical analysis of known theories for mathematically describing the motion of multi-phase (two-phase) systems and methods for averaging the hydrodynamic characteristics of a turbulent flow are given. The procedure for closing the equations systems of hydromechanics of multi-phase flows proposed in existing works is carried out within the framework of semi-empirical theories of turbulence. In nature, the vast majority of multi-phase (two-phase, inhomogeneous) mixtures exhibit turbulent behavior, making its study a crucial practical task. The mathematical description of the motion of a turbulent multi-phase flow relies on stylized laws of mechanics. The methods of operational analysis proposed at various times by different researchers for the mathematical description of the motion of a multi-phase (two-phase) flow have varying degrees of approximation and certain limited areas of application. One of the main challenges in formulating differential equations for the motion of a turbulent multi-phase (two-phase, suspension-carrying) flow is the fact that in a turbulent flow of a mixture, where the characteristics of the flow change chaotically and randomly over time and at each point in space, both in magnitude and in direction, there are surfaces with weak and strong discontinuities. Consequently, the actual values of velocity and pressure of a multi-phase flow, strictly speaking, cannot be considered continuous functions of the coordinates of space and time throughout the entire region occupied by the mixture.
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来源期刊
Nafta-Gaz
Nafta-Gaz ENGINEERING, PETROLEUM-
CiteScore
0.80
自引率
60.00%
发文量
81
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