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Simulation and scaling analysis of periodic surfaces with small-scale roughness in turbulent Ekman flow 埃克曼湍流中具有小尺度粗糙度的周期性表面的模拟和缩放分析
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-30 DOI: 10.1017/jfm.2024.542
Jonathan Kostelecky, Cedrick Ansorge
Roughness of the surface underlying the atmospheric boundary layer causes departures of the near-surface scalar and momentum transport in comparison with aerodynamically smooth surfaces. Here, we investigate the effect of <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline1.png"/> <jats:tex-math>$56times 56$</jats:tex-math> </jats:alternatives> </jats:inline-formula> homogeneously distributed roughness elements on bulk properties of a turbulent Ekman flow. Direct numerical simulation in combination with an immersed boundary method is performed for fully resolved, three-dimensional roughness elements. The packing density is approximately <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline2.png"/> <jats:tex-math>$10,%$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and the roughness elements have a mean height in wall units of <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline3.png"/> <jats:tex-math>$10 lesssim H^+ lesssim 40$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. According to their roughness Reynolds numbers, the cases are transitionally rough, although the roughest case is on the verge of being fully rough. We derive the friction of velocity and of the passive scalar through vertical integration of the respective balances. Thereby, we quantify the enhancement of turbulent activity with increasing roughness height and find a scaling for the friction Reynolds number that is verified up to <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline4.png"/> <jats:tex-math>$Re_tau approx 2700$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. The higher level of turbulent activity results in a deeper logarithmic layer for the rough cases and an increase of the near-surface wind veer in spite of higher <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline5.png"/> <jats:tex-math>$Re_tau$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. We estimate the von Kármán constant for the horizontal velocity <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline6.png"/> <jats:tex-math>$kappa _{m}=0.42$</jats:tex-math> </jats:alternatives> </jats:inline-formula> (offset <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005421_inline7.png"/> <jats:tex-math>$A=5.44$</jats:tex-
与空气动力学光滑表面相比,大气边界层下表面的粗糙度会导致近表面标量和动量传输的偏离。在这里,我们研究了 56 次 56 元均匀分布的粗糙度元素对湍流埃克曼流体质的影响。结合沉浸边界法对完全解析的三维粗糙度元素进行了直接数值模拟。堆积密度约为 $10,%$,粗糙度元素以壁为单位的平均高度为 $10 lesssim H^+ lesssim 40$。根据其粗糙度雷诺数,这些情况都是过渡粗糙,尽管最粗糙的情况濒临完全粗糙。我们通过对各自的平衡进行垂直积分,得出了速度和被动标量的摩擦力。因此,我们量化了湍流活动随粗糙度高度增加而增强的情况,并找到了摩擦雷诺数的缩放比例,该比例最高可达 $Re_tau approx 2700$。更高水平的湍流活动导致粗糙度情况下的对数层更深,并且尽管Re_tau$更高,近表面风偏也会增加。我们估算了水平速度 $kappa _{m}=0.42$ (偏移 $A=5.44$)和被动标量 $kappa _{h}=0.35$ (偏移 $mathbb {A}=4.2$ )的冯卡尔曼常数。我们发现在对数层的粗糙壁缩放下,数据会发生精确的坍缩,这也产生了动量($z_{0{m}}$)和被动标量($z_{0{h}}$)的粗糙度参数$z$-无缩放。
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引用次数: 0
Onset of turbulence in rotor–stator cavity flows 转子-定子空腔流中湍流的发生
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-28 DOI: 10.1017/jfm.2024.536
Yaguang Xie, Qiang Du, Lei Xie, Zhicheng Wang, Siyi Li
Numerous studies have indicated that turbulence typically initiates along the boundary layer of the stationary disk within a rotor–stator cavity. To describe the transition process to turbulence on the stationary side of a closed rotor–stator cavity, a comprehensive approach combining global linear stability analysis with direct numerical simulation was adopted in the present study. The proposed model aligns with that of Yim et al. (J. Fluid Mech., vol. 848, 2018, pp. 631–647), who investigated the stability characteristics of the rotating-disk boundary layer in a rotor–stator cavity. In order to achieve a stable inflow for the stationary-disk boundary layer, we rotate the shroud together with the rotating disk. Through careful global stability analysis, the predominant spiral mode exhibiting the highest instability in the boundary layer of the stationary disk was discerned, corroborating observations from simulations. Initially, the spiral mode undergoes linear amplification, reaches a state of linear saturation and enters the nonlinear regime. Following nonlinear saturation in the flow field, a circular wave mode arises due to the influence of mean flow distortion. As the Reynolds number attained a sufficiently high level, the interplay between the downstream-propagating circular mode and spiral mode amplified disturbances in the boundary layer of the stationary disk, ultimately leading to the development of localised turbulence at the mid-radius of the rotor–stator cavity. Notably, the present study is the first to elucidate the coexistence of laminar–transitional–turbulent flow states in the stationary-disk boundary layer through direct numerical simulations.
大量研究表明,湍流通常是沿着转子-定子空腔内静止盘的边界层开始的。为了描述封闭转子-定子空腔静止侧向湍流的过渡过程,本研究采用了全局线性稳定性分析与直接数值模拟相结合的综合方法。提出的模型与 Yim 等人(《流体力学》,第 848 卷,2018 年,第 631-647 页)研究转子-定子空腔中旋转盘边界层稳定性特征的模型一致。为了实现静止盘边界层的稳定流入,我们将护罩与旋转盘一起旋转。通过细致的全局稳定性分析,我们确定了静止盘边界层中不稳定性最高的主要螺旋模式,这与模拟观测结果相吻合。最初,螺旋模式经过线性放大,达到线性饱和状态,并进入非线性状态。流场非线性饱和后,由于平均流变形的影响,出现了圆波模式。当雷诺数达到足够高的水平时,顺流传播的圆波模式和螺旋模式之间的相互作用放大了静止圆盘边界层的扰动,最终导致转子-定子空腔中半径处出现局部湍流。值得注意的是,本研究首次通过直接数值模拟阐明了静止盘边界层中层流-过渡流-湍流共存的流动状态。
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引用次数: 0
The starting vortices generated by bodies with sharp and straight edges in a viscous fluid 粘性流体中尖锐和笔直边缘的物体产生的起始涡流
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-28 DOI: 10.1017/jfm.2024.515
John E. Sader, Wei Hou, Edward M. Hinton, D.I. Pullin, Tim Colonius
A two-dimensional body that moves suddenly in a viscous fluid can instantly generate vortices at its sharp edges. Recent work using inviscid flow theory, based on the Birkhoff–Rott equation and the Kutta condition, predicts that the ‘starting vortices’ generated by the sharp and straight edges of a body – i.e. the vortices formed immediately after motion begins – can be one of three distinct self-similar types. We explore the existence of these starting vortices for a flat plate and two symmetric Joukowski aerofoils immersed in a viscous fluid, using high-fidelity direct numerical simulations (DNS) of the Navier–Stokes equations. A lattice Green's function method is employed and simulations are performed for chord Reynolds numbers ranging from 5040 to 45 255. Vortices generated at the leading and trailing edges of the flat plate show agreement with the derived inviscid theory, for which a detailed assessment is reported. Agreement is also observed for the two symmetric Joukowski aerofoils, demonstrating the utility of the inviscid theory for arbitrary bodies. While this inviscid theory predicts an abrupt transition between the starting-vortex types, DNS shows a smooth transition. This behaviour occurs for all Reynolds numbers and is related to finite-time effects – there is a maximal time for which the (self-similar) starting vortices exist. We confirm the inviscid prediction that the leading-edge starting vortex of a flat plate can be suppressed dynamically. This has implications for the performance of low-speed aircraft such as model aeroplanes, micro air vehicles and unmanned air vehicles.
在粘性流体中突然移动的二维物体会在其锐利边缘瞬间产生涡流。根据基于伯克霍夫-罗特方程和库塔条件的不粘性流理论,最近的研究预测,由体的锐边和直边产生的 "起始涡"--即运动开始后立即形成的涡--可以是三种不同的自相似类型之一。我们利用纳维-斯托克斯方程的高保真直接数值模拟 (DNS),探索了浸没在粘性流体中的平板和两个对称焦科夫斯基气膜是否存在这些起始涡流。模拟采用格点格林函数法,弦雷诺数从 5040 到 45 255 不等。在平板的前缘和后缘产生的涡流与推导出的无粘性理论一致,并对此进行了详细评估。在两个对称的 Joukowski 气膜上也观察到了一致性,这证明了无粘性理论对任意物体的实用性。虽然这种不粘性理论预测起始涡流类型之间会突然过渡,但 DNS 却显示出平稳的过渡。在所有雷诺数下都会出现这种现象,这与有限时间效应有关--(自相似)起始涡存在的最大时间是有限的。我们证实了不粘性预言,即平板的前缘起始涡流可以被动态抑制。这对低速飞行器(如模型飞机、微型飞行器和无人驾驶飞行器)的性能有影响。
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引用次数: 0
Obstacle arrangement can control flows through porous obstructions 障碍物布置可控制通过多孔障碍物的水流
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-28 DOI: 10.1017/jfm.2024.510
Fei He, Hongwei An, Marco Ghisalberti, Scott Draper, Chengjiao Ren, Paul Branson, Liang Cheng
Previous work suggests that the arrangement of elements in an obstruction may influence the bulk flow velocity through the obstruction, but the physical mechanisms for this influence are not yet clear. This is the motivation for this study, where direct numerical simulation is used to investigate flow through an array of cylinders at a resolution sufficient to observe interactions between wakes of individual elements. The arrangement is altered by varying the gap ratio $G/d$ (1.2 – 18, G is the distance between two adjacent cylinders, d is the cylinder diameter), array-to-element diameter ratio $D/d$ (3.6 – 200, D is the array diameter), and incident flow angle ( $0^{circ} - 30^{circ}$ ). Depending on the element arrangement, it is found that the average root-mean-square lift and drag coefficients can vary by an order of magnitude, whilst the average time-mean drag coefficient of individual cylinders ( $overline{C_{d}}$ ), and the bulk velocity are found to vary by up to $50,%$ and a factor of 2, respectively. These arrangement effects are a consequence of the variation in flow and drag characteristics of individual cylinders within the array. The arrangement effects become most critical in the intermediate range of flow blockage parameter $mathit{Gamma_{D}^{prime}} = 0.5-1.5$ (
以往的研究表明,障碍物中元件的排列可能会影响通过障碍物的整体流速,但这种影响的物理机制尚不清楚。因此,本研究采用直接数值模拟来研究流经圆柱体阵列的情况,其分辨率足以观察到单个元件之间的相互作用。通过改变间隙比 $G/d$(1.2 - 18,G 为两个相邻圆柱体之间的距离,d 为圆柱体直径)、阵列与元件直径比 $D/d$(3.6 - 200,D 为阵列直径)和入射流角($0^{circ} - 30^{circ}$ )来改变排列方式。根据不同的元素排列,平均均方根升力和阻力系数可能会有一个数量级的变化,而单个圆柱体的平均时间均值阻力系数($overline{C_{d}}$)和体积速度的变化分别高达 $50,%$ 和 2 倍。这些排列效应是阵列中单个圆柱体的流动和阻力特性变化的结果。在流动阻塞参数 $mathit{Gamma_{D}^{prime}} = 0.5-1.5$ ($mathit{Gamma_{D}^{prime}}=overline{C_{d}}aD/(1-phi)$,其中 a 是单位体积的正面元件面积,$phi$ 是固体体积分数)的中间范围内,由于元件尺度流动特性的高度可变性,排列效应变得最为关键。在所模拟的所有布置范围内,可以确认体积速度受流动阻塞参数的支配,但只有在阻力系数包含布置效应的情况下才受其支配。利用这些结果,本文提出了一个框架,用于描述和预测通过各种排列阵列的流动。
{"title":"Obstacle arrangement can control flows through porous obstructions","authors":"Fei He, Hongwei An, Marco Ghisalberti, Scott Draper, Chengjiao Ren, Paul Branson, Liang Cheng","doi":"10.1017/jfm.2024.510","DOIUrl":"https://doi.org/10.1017/jfm.2024.510","url":null,"abstract":"Previous work suggests that the arrangement of elements in an obstruction may influence the bulk flow velocity through the obstruction, but the physical mechanisms for this influence are not yet clear. This is the motivation for this study, where direct numerical simulation is used to investigate flow through an array of cylinders at a resolution sufficient to observe interactions between wakes of individual elements. The arrangement is altered by varying the gap ratio <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2ab.png\"/> <jats:tex-math>$G/d$</jats:tex-math> </jats:alternatives> </jats:inline-formula> (1.2 – 18, <jats:italic>G</jats:italic> is the distance between two adjacent cylinders, <jats:italic>d</jats:italic> is the cylinder diameter), array-to-element diameter ratio <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2gf.png\"/> <jats:tex-math>$D/d$</jats:tex-math> </jats:alternatives> </jats:inline-formula> (3.6 – 200, <jats:italic>D</jats:italic> is the array diameter), and incident flow angle (<jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2b.png\"/> <jats:tex-math>$0^{circ} - 30^{circ}$</jats:tex-math> </jats:alternatives> </jats:inline-formula>). Depending on the element arrangement, it is found that the average root-mean-square lift and drag coefficients can vary by an order of magnitude, whilst the average time-mean drag coefficient of individual cylinders (<jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2c.png\"/> <jats:tex-math>$overline{C_{d}}$</jats:tex-math> </jats:alternatives> </jats:inline-formula>), and the bulk velocity are found to vary by up to <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2d.png\"/> <jats:tex-math>$50,%$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and a factor of 2, respectively. These arrangement effects are a consequence of the variation in flow and drag characteristics of individual cylinders within the array. The arrangement effects become most critical in the intermediate range of flow blockage parameter <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S002211202400510X_inline2e.png\"/> <jats:tex-math>$mathit{Gamma_{D}^{prime}} = 0.5-1.5$</jats:tex-math> </jats:alternatives> </jats:inline-formula> (<jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S00221120","PeriodicalId":15853,"journal":{"name":"Journal of Fluid Mechanics","volume":"175 1","pages":""},"PeriodicalIF":3.7,"publicationDate":"2024-08-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142207440","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Trading particle shape with fluid symmetry: on the mobility matrix in 3-D chiral fluids 粒子形状与流体对称性的交易:三维手性流体中的流动矩阵
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.535
Tali Khain, Michel Fruchart, Colin Scheibner, Thomas A. Witten, Vincenzo Vitelli
Chiral fluids – such as fluids under rotation or a magnetic field as well as synthetic and biological active fluids – flow in a different way than ordinary ones. Due to symmetries broken at the microscopic level, chiral fluids may have asymmetric stress and viscosity tensors, for example giving rise to a hydrostatic torque or non-dissipative (odd) and parity-violating viscosities. In this article, we investigate the motion of rigid bodies in such an anisotropic fluid in the incompressible Stokes regime through the mobility matrix, which encodes the response of a solid body to forces and torques. We demonstrate how the form of the mobility matrix, which is usually determined by particle geometry, can be analogously controlled by the symmetries of the fluid. By computing the mobility matrix for simple shapes in a three-dimensional (3-D) anisotropic chiral fluid, we predict counterintuitive phenomena such as motion at an angle to the direction of applied forces and spinning under the force of gravity.
手性流体(如旋转或磁场下的流体以及合成和生物活性流体)的流动方式与普通流体不同。由于对称性在微观层面被破坏,手性流体可能具有不对称的应力和粘度张量,例如产生流体静力学力矩或非耗散(奇数)和违反奇偶性的粘度。在本文中,我们通过流动性矩阵研究了不可压缩斯托克斯体系中各向异性流体中的刚体运动,流动性矩阵编码了实体对力和扭矩的响应。我们演示了通常由粒子几何形状决定的流动性矩阵的形式如何类似地受流体对称性的控制。通过计算三维(3-D)各向异性手性流体中简单形状的流动性矩阵,我们预测了一些反直觉现象,如与外力方向成一定角度的运动以及在重力作用下的旋转。
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引用次数: 0
Turbulence effect on disk settling dynamics 湍流对圆盘沉降动力学的影响
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.534
Amy Tinklenberg, Michele Guala, Filippo Coletti
Turbulence can have a strong effect on the fall speed of snowflakes and ice crystals. In this experimental study, the behaviour of thin disks falling in homogeneous turbulence is investigated, in a range of parameters relevant to plate crystals. Disks ranging in diameter from 0.3 to 3 mm, and in Reynolds number $Re = 10unicode{x2013}435$ , are dispersed in two air turbulence levels, with velocity fluctuations comparable to the terminal velocity. For each case, thousands of trajectories are captured and reconstructed by high-speed laser imaging, allowing for statistical analysis of the translational and rotational dynamics. Air turbulence reduces the disk terminal velocities by up to 35 %, with the largest diameters influenced most significantly, which is primarily attributed to drag nonlinearity. This is evidenced by large lateral excursions of the trajectories, which correlate with cross-flow-induced drag enhancement as reported previously for falling spheres and rising bubbles. As the turbulence intensity is increased, flat-falling behaviour is progressively eliminated and tumbling becomes prevalent. The rotation rates of the tumbling disks, however, remain similar to those displayed in still air. This is due to their large moment of inertia compared to the surrounding fluid, in stark contrast with studies conducted in water. In fact, the observed reduction of settling velocity is opposite to previous findings on disks falling in turbulent water. This emphasizes the importance of the solid-to-fluid density ratio in analogous experiments that aim to mimic the behaviour of frozen hydrometeors.
湍流对雪花和冰晶的下落速度有很大影响。在这项实验研究中,研究了薄圆盘在均质湍流中的下落行为,其参数范围与板状晶体相关。直径在 0.3 到 3 毫米之间、雷诺数为 $Re = 10unicode{x2013}435$ 的圆盘分散在两个空气湍流级别中,其速度波动与末端速度相当。在每种情况下,通过高速激光成像捕捉并重建了数千条轨迹,从而对平移和旋转动力学进行了统计分析。空气湍流使圆盘的末端速度降低了 35%,最大直径的圆盘受到的影响最大,这主要归因于阻力非线性。轨迹的大幅横向偏移证明了这一点,这与之前报告的下降球体和上升气泡的横流诱导阻力增强相关。随着湍流强度的增加,平落行为逐渐消失,翻滚变得普遍。然而,翻滚盘的旋转率仍与静止空气中的旋转率相似。这是因为与周围流体相比,它们的惯性矩较大,这与在水中进行的研究形成了鲜明对比。事实上,观察到的沉降速度降低与之前在湍流水中的圆盘沉降研究结果相反。这强调了在旨在模拟冰冻水介质行为的类似实验中,固体与流体密度比的重要性。
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引用次数: 0
Vibration-induced wall–bubble interactions under zero-gravity conditions 零重力条件下由振动引起的壁泡相互作用
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.541
D.V. Lyubimov, T.P. Lyubimova, S. Meradji, B. Roux
This work is devoted to a theoretical and numerical study of the dynamics of a two-phase system vapour bubble in equilibrium with its liquid phase under translational vibrations in the absence of gravity. The bubble is initially located in the container centre. The liquid and vapour phases are considered as viscous and incompressible. Analysis focuses on the vibrational conditions used in experiments with the two-phase system SF $_6$ in the MIR space station and with the two-phase system para-Hydrogen (p-H $_2$ ) under magnetic compensation of Earth's gravity. These conditions correspond to small-amplitude high-frequency vibrations. Under vibrations, additionally to the forced oscillations, an average displacement of the bubble to the wall is observed due to an average vibrational attraction force related to the Bernoulli effect. Vibrational conditions for SF $_6$ correspond to much smaller average vibrational force (weak vibrations) than for p-H $_2$ (strong vibrations). For weak vibrations, the role of the initial vibration phase is crucial. The difference in the behaviour at different initial phases is explained using a simple mechanical model. For strong vibrations, the average displacement to the wall stops when the bubble reaches a quasi-equilibrium position where the resulting average force is zero. At large vibration velocity amplitudes this position is near the wall where the bubble performs only forced oscillations. At moderate vibration velocity amplitudes the bubble average displacement stops at a finite distance from the wall, then large-scale damped oscillations around this position accompanied by forced oscillations are observed. Bubble shape oscillations and the parametric resonance of forced oscillations are also studied.
这项研究致力于在无重力条件下,对处于与液相平衡状态的两相系统汽泡在平移振动下的动力学进行理论和数值研究。气泡最初位于容器中心。液相和汽相被认为是粘性和不可压缩的。分析的重点是在 MIR 空间站中两相体系 SF $_6$ 的实验中使用的振动条件,以及在地球引力的磁补偿下两相体系对位氢(p-H $_2$ )的实验中使用的振动条件。这些条件对应于小振幅高频振动。在振动条件下,除了受迫振荡之外,由于与伯努利效应有关的平均振动吸引力,还观察到气泡向壁面的平均位移。SF_6$ 的振动条件对应的平均振动力(弱振动)要比 p-H_2$ 的小得多(强振动)。对于弱振动,初始振动阶段的作用至关重要。我们可以用一个简单的机械模型来解释不同初始阶段的行为差异。对于强振动,当气泡达到所产生的平均力为零的准平衡位置时,气泡壁的平均位移就会停止。在振动速度振幅较大时,该位置靠近气泡仅进行受迫振荡的壁面。在中等振动速度振幅下,气泡的平均位移停止在离壁的有限距离处,然后在该位置附近观察到大规模的阻尼振荡,并伴有受迫振荡。此外,还研究了气泡形状振荡和受迫振荡的参数共振。
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引用次数: 0
Non-universality and dissipative anomaly in compressible magnetohydrodynamic turbulence 可压缩磁流体动力学湍流中的非普遍性和耗散异常
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.545
Cheng Li, Yan Yang, William H. Matthaeus, Bin Jiang, Minping Wan, Shiyi Chen
We systematically study the dissipative anomaly in compressible magnetohydrodynamic (MHD) turbulence using direct numerical simulations, and show that the total dissipation remains finite as viscosity diminishes. The dimensionless dissipation rate $mathcal {C}_{varepsilon }$ fits well with the model $mathcal {C}_{varepsilon } = mathcal {C}_{varepsilon,infty } + mathcal {D}/R_L^-$ for all levels of flow compressibility considered here, where $R_L^-$ is the generalized large-scale Reynolds number. The asymptotic value $mathcal {C}_{varepsilon,infty }$ describes the total energy transfer flux, and decreases with increase of the flow compressibility, indicating non-universality of the dimensionless dissipation rate in compressible MHD turbulence. After introducing an empirically modified dissipation rate, the data from compressible cases collapse to a form similar to the incompressible MHD case depending only on the modified Reynolds number.
我们利用直接数值模拟系统地研究了可压缩磁流体动力学(MHD)湍流中的耗散异常,结果表明总耗散随粘度减小而保持有限。无量纲耗散率 $mathcal {C}_{varepsilon }$ 与模型 $mathcal {C}_{varepsilon } 非常吻合。= mathcal {C}_{varepsilon,infty }+ mathcal {D}/R_L^-$ 适用于本文考虑的所有流动压缩性水平,其中 $R_L^-$ 是广义大尺度雷诺数。渐近值 $mathcal {C}_{varepsilon,infty }$ 描述了总的能量传递通量,并随着流动压缩性的增加而减小,表明可压缩 MHD 湍流中无量纲耗散率的非普遍性。在引入根据经验修正的耗散率之后,可压缩情况下的数据坍缩为与不可压缩 MHD 情况类似的形式,仅取决于修正的雷诺数。
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引用次数: 0
Mixing as a correlated aggregation process 作为相关聚合过程的混合
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.537
J. Heyman, E. Villermaux, P. Davy, T. Le Borgne
Mixing describes the process by which solutes evolve from an initial heterogeneous state to uniformity under the stirring action of a fluid flow. Fluid stretching forms thin scalar lamellae that coalesce due to molecular diffusion. Owing to the linearity of the advection–diffusion equation, coalescence can be envisioned as an aggregation process. Here, we demonstrate that in smooth two-dimensional chaotic flows, mixing obeys a correlated aggregation process, where the spatial distribution of the number of lamellae in aggregates is highly correlated with their elongation, and is set by the fractal properties of the advected material lines. We show that the presence of correlations makes mixing less efficient than a completely random aggregation process because lamellae with similar elongations and scalar levels tend to remain isolated from each other. We show that correlated aggregation is uniquely determined by a single exponent that quantifies the effective number of random aggregation events. These findings expand aggregation theories to a larger class of systems, which have relevance to various fundamental and applied mixing problems.
混合描述了在流体流动的搅拌作用下,溶质从最初的异质状态演变为均匀状态的过程。流体拉伸形成薄薄的标量薄片,这些薄片由于分子扩散而凝聚在一起。由于平流-扩散方程的线性关系,凝聚可以看作是一个聚集过程。在这里,我们证明了在平滑的二维混沌流中,混合遵从一个相关的聚集过程,聚集体中薄片数量的空间分布与它们的伸长高度相关,并且由平流材料线的分形特性决定。我们的研究表明,相关性的存在使得混合的效率低于完全随机的聚集过程,因为具有相似伸长率和标量水平的薄片往往会相互隔离。我们的研究表明,相关聚集是由单一指数唯一决定的,该指数量化了随机聚集事件的有效数量。这些发现将聚集理论扩展到了更大的系统类别,与各种基础和应用混合问题息息相关。
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引用次数: 0
Direct numerical simulation of 45° oblique flow past surface-mounted square cylinder 45° 斜向流经表面安装方形圆筒的直接数值模拟
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.554
Dung Viet Duong, Luc Van Nguyen, Duc Van Nguyen, Truong Cong Dinh, Lavi Rizki Zuhal, Long Ich Ngo
Comprehensive coherent structures around a surface-mounted low aspect ratio square cylinder in uniform flow with an oblique angle of $45^{circ }$ were investigated for cylinder-width-based Reynolds numbers of 3000 and 10 000 by direct numerical simulation based on a topology-confined mesh refinement framework. High-resolution simulations and the critical-point concept were scrutinized to reveal for the first time the reasonable and compatible topologies of flow separation and complete near-wall structures, due to their extensive impact on various engineering applications. Large-scale horseshoe vortices are observed at two notable foci in the viscous sublayer. Within this layer, a wall-parallel jet is formed by downflow intruding into the bottom surface at the half-saddle point, then deflecting in the upstream direction and finally penetrating the bottom surface until the half-saddle point. A pair of conical vortices on the cylinder's top surface switch themselves on two sides of the square cylinder, where the switching frequency is identical with that of the sway of the side shear layer. The undulation of the Kelvin–Helmholtz instability is identified in the instantaneous development of a conical vortex and side shear layer, where the scaling of the ratio of the Kelvin–Helmholtz and von Kármán frequencies follows the power-law relation obtained by Lander et al. (J. Fluid Mech., vol. 849, 2018, pp. 1096–1119). Large-scale arch-shaped vortex is often detected in the intermediate wake region of a square cylinder, involving two interconnected portions, such as the leg portion separated from leeward surfaces and head portion rolled up from the top surface. The leg portion of the arch-shaped vortex was rooted by two foci near the bottom-surface plane.
通过基于拓扑约束网格细化框架的直接数值模拟,研究了在斜角为 $45^{circ }$ 的均匀流中,基于圆柱体宽度的雷诺数为 3000 和 10 000 时,表面安装的低纵横比方形圆柱体周围的综合相干结构。由于高分辨率模拟和临界点概念对各种工程应用的广泛影响,研究首次揭示了流体分离和完整近壁结构的合理兼容拓扑结构。在粘性子层的两个显著焦点处观察到了大尺度马蹄涡。在这一层中,下流在半鞍点侵入底面,然后向上游方向偏转,最后穿透底面直至半鞍点,形成了与壁面平行的射流。圆柱体顶面的一对锥形涡流在方形圆柱体的两侧切换,切换频率与侧剪切层的摇摆频率相同。开尔文-赫尔姆霍兹不稳定性的起伏在锥形涡旋和侧剪切层的瞬时发展中得以确定,其中开尔文-赫尔姆霍兹频率和冯-卡尔曼频率的比例关系遵循 Lander 等人获得的幂律关系(《流体力学》,第 849 卷,2018 年,第 1096-1119 页)。在方形圆柱体的中间尾流区域经常检测到大尺度拱形涡旋,涉及两个相互连接的部分,如与背风面分离的腿部和从顶面卷起的头部。拱形涡旋的腿部由靠近底面平面的两个焦点构成。
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引用次数: 0
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Journal of Fluid Mechanics
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