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One-winged butterflies: mode selection for azimuthal magnetorotational instability by thermal convection 单翼蝴蝶:热对流方位磁定向不稳定性的模式选择
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-27 DOI: 10.1017/jfm.2024.517
Ashish Mishra, George Mamatsashvili, Martin Seilmayer, Frank Stefani
The effects of thermal convection on turbulence in accretion discs, and particularly its interplay with the magnetorotational instability (MRI), are of significant astrophysical interest. Despite extensive theoretical and numerical studies, such an interplay has not been explored experimentally. We conduct linear analysis of the azimuthal version of MRI (AMRI) in the presence of thermal convection and compare the results with our experimental data published before. We show that the critical Hartmann number ( $Ha$ ) for the onset of AMRI is reduced by convection. Importantly, convection breaks symmetry between $m = pm 1$ instability modes ( $m$ is the azimuthal wavenumber). This preference for one mode over the other makes the AMRI wave appear as a ‘one-winged butterfly’.
热对流对吸积盘湍流的影响,特别是它与磁导不稳定性(MRI)的相互作用,具有重大的天体物理学意义。尽管进行了大量的理论和数值研究,但这种相互作用尚未得到实验探索。我们对存在热对流情况下的方位磁不稳定性(AMRI)进行了线性分析,并将结果与之前公布的实验数据进行了对比。我们的研究表明,对流会降低 AMRI 发生的临界哈特曼数($Ha$)。重要的是,对流打破了 $m =pm 1$ 不稳定模式($m$ 是方位角波数)之间的对称性。这种对一种模式的偏好使 AMRI 波看起来像一只 "单翼蝴蝶"。
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引用次数: 0
Turbulent jet theory via Lie symmetry analysis: the free plane jet 通过李对称分析的湍流射流理论:自由平面射流
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.527
Nadeem A. Malik, Fazle Hussain
A theory of incompressible turbulent plane jets (TPJs) is proposed by advancing an improved boundary layer approximation over the limiting classical – retaining more terms in the momentum balance equations. A pressure deficit inside the jet (with respect to the ambient) must exist due to transverse turbulence (Miller & Comings, <jats:italic>J. Fluid Mech.</jats:italic>, vol. 3, 1957, pp. 1–16; Hussain & Clarke, <jats:italic>Phys. Fluids</jats:italic>, vol. 20, 1977, pp. 1416–1426). Contrary to the universally accepted invariance of the total momentum flux <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline1.png"/> <jats:tex-math>$J_T(x)$</jats:tex-math> </jats:alternatives> </jats:inline-formula> (non-dimensionalized by its inlet value) as a function of the streamwise distance <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline2.png"/> <jats:tex-math>$x$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, we prove that <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline3.png"/> <jats:tex-math>$J_T(x) >1$</jats:tex-math> </jats:alternatives> </jats:inline-formula> – a condition that all TPJs must satisfy; surprisingly, prior theories and most experiments do not satisfy this condition. This motivated us to apply Lie symmetry analysis with translational and dilatational transformations of the modified equations (incorporating <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline4.png"/> <jats:tex-math>$J_T>1$</jats:tex-math> </jats:alternatives> </jats:inline-formula>), which yields scaling laws for key jet measures: the mean streamwise and transverse velocities <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline5.png"/> <jats:tex-math>$U(x,y)$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline6.png"/> <jats:tex-math>$V(x,y)$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, the turbulence intensities, the Reynolds shear stress <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005275_inline8.png"/> <jats:tex-math>$-rho ,overline {u'v'}(x,y)$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, the mean pressure <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org
提出了不可压缩湍流平面喷流(TPJs)理论,该理论通过改进边界层近似来超越传统的限制--在动量平衡方程中保留更多的项。由于横向湍流,喷流内部(相对于环境)必须存在压力不足(Miller & Comings,《流体力学》,第 3 卷,1957 年,第 1-16 页;Hussain & Clarke,《流体物理学》,第 20 卷,1977 年,第 1416-1426 页)。与普遍接受的总动量通量 $J_T(x)$(非以其入口值为维度)作为流向距离 $x$ 的函数的不变性相反,我们证明了 $J_T(x) >1$ - 所有 TPJ 都必须满足的条件;令人惊讶的是,先前的理论和大多数实验都不满足这个条件。这促使我们对修正方程(包含 $J_T>1$ )进行平移和扩张变换,应用李对称分析,从而得出关键射流量度的缩放定律:平均流向和横向速度 $U(x,y)$ 和 $V(x,y)$ 、湍流强度、雷诺切应力 $-rho ,overline {u'v'}(x,y)$ 、平均压力 $P(x,y)$ 等。满足 $J_T(x)>1$ 的实验验证了我们对所有射流测量值的预测,其中包括 $U$ 、$V$ 和 $-rhooverline {u'v'}$ 的剖面。我们进一步预测 $U sim x^{-0.24}$ 、 $V sim x^{-0.45}$ 、 $-rho ,overline {u'v'}sim x^{-0.69}$ 、质量通量 $Q_m sim x^{0.55}$ 以及 $J_T$ 会增加到大约 1.5。与经典的线性射流扩散相反,我们发现了亚线性扩散,射流半宽的增长速度为$b(x)sim x^{0.79}$,表明射流更窄。我们的预测与文献报道的大多数结果明显不同。这些矛盾要求我们重新审视涉及精心设计的设施和边界条件以及高分辨率模拟的射流研究。
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引用次数: 0
Prandtl number dependence of flow topology in quasi-two-dimensional turbulent Rayleigh–Bénard convection 准二维湍流雷利-贝纳德对流中流动拓扑的普朗特数依赖性
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.550
Ze-Hao Wang, Xin Chen, Ao Xu, Heng-Dong Xi
To date, a comprehensive understanding of the influence of the Prandtl number (<jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline1.png"/> <jats:tex-math>$Pr$</jats:tex-math> </jats:alternatives> </jats:inline-formula>) on flow topology in turbulent Rayleigh–Bénard convection (RBC) remains elusive. In this study, we present an experimental investigation into the evolution of flow topology in quasi-two-dimensional turbulent RBC with <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline4.png"/> <jats:tex-math>$7.0 leq Pr leq 244.2$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline5.png"/> <jats:tex-math>$2.03times 10^{8} leq Ra leq 2.81times 10^{9}$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. Particle image velocimetry (PIV) measurements reveal the flow transitions from multiple-roll state to single-roll state with increasing <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline6.png"/> <jats:tex-math>$Ra$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, and the transition is hindered with increasing <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline7.png"/> <jats:tex-math>$Pr$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, i.e. the transitional Rayleigh number <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline8.png"/> <jats:tex-math>$Ra_t$</jats:tex-math> </jats:alternatives> </jats:inline-formula> increases with <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline9.png"/> <jats:tex-math>$Pr$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. We mapped out a phase diagram on the flow topology change on <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline10.png"/> <jats:tex-math>$Ra$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005500_inline11.png"/> <jats:tex-math>$Pr$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, and identified the scaling of <jats:inline-formula> <jats:alternatives> <jats:in
迄今为止,关于普朗特数($Pr$)对湍流雷利-贝纳德对流(RBC)中流动拓扑的影响的全面理解仍未形成。在本研究中,我们对准二维湍流雷利-贝纳德对流(RBC)中的流动拓扑演变进行了实验研究,Pr leq 244.2$和Ra leq 10^{8} 的值分别为$7.0和$2.03。leq Ra leq 2.81 (乘以 10^{9}$ )。粒子图像测速仪(PIV)测量显示,随着 $Ra$ 的增加,流动从多辊态过渡到单辊态,并且随着 $Pr$ 的增加,过渡受阻,即过渡瑞利数 $Ra_t$ 随着 $Pr$ 的增加而增加。我们绘制了流动拓扑变化在 $Ra$ 和 $Pr$ 上的相图,并确定了 $Ra_t$ 在 $Pr$ 上的缩放:在低 $Pr$ 范围内为 $Ra_t sim Pr^{0.93}$,而在高 $Pr$ 范围内为 $Ra_t sim Pr^{3.3}$。低Pr$范围内的缩放与我们之前研究中提出的能量耗散时间和羽流移动时间的平衡模型是一致的,而高Pr$范围内的缩放则意味着一种新的调控机制。我们首次通过全场 PIV 速度测量获得了 $Re$ 对 $Ra$ 和 $Pr$ 的比例关系,即 $Re sim Ra^{0.63},Pr^{-0.87}$ 。我们还提出,水平速度的增加会促进大尺度环流(LSC)的形成,尤其是在高 Pr$ 的情况下。通过小角度倾斜对流单元,引入水平驱动力$Ra_H$,实现大尺度环流,验证了我们的提议。
{"title":"Prandtl number dependence of flow topology in quasi-two-dimensional turbulent Rayleigh–Bénard convection","authors":"Ze-Hao Wang, Xin Chen, Ao Xu, Heng-Dong Xi","doi":"10.1017/jfm.2024.550","DOIUrl":"https://doi.org/10.1017/jfm.2024.550","url":null,"abstract":"To date, a comprehensive understanding of the influence of the Prandtl number (&lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline1.png\"/&gt; &lt;jats:tex-math&gt;$Pr$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;) on flow topology in turbulent Rayleigh–Bénard convection (RBC) remains elusive. In this study, we present an experimental investigation into the evolution of flow topology in quasi-two-dimensional turbulent RBC with &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline4.png\"/&gt; &lt;jats:tex-math&gt;$7.0 leq Pr leq 244.2$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; and &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline5.png\"/&gt; &lt;jats:tex-math&gt;$2.03times 10^{8} leq Ra leq 2.81times 10^{9}$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;. Particle image velocimetry (PIV) measurements reveal the flow transitions from multiple-roll state to single-roll state with increasing &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline6.png\"/&gt; &lt;jats:tex-math&gt;$Ra$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;, and the transition is hindered with increasing &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline7.png\"/&gt; &lt;jats:tex-math&gt;$Pr$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;, i.e. the transitional Rayleigh number &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline8.png\"/&gt; &lt;jats:tex-math&gt;$Ra_t$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; increases with &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline9.png\"/&gt; &lt;jats:tex-math&gt;$Pr$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;. We mapped out a phase diagram on the flow topology change on &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline10.png\"/&gt; &lt;jats:tex-math&gt;$Ra$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; and &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005500_inline11.png\"/&gt; &lt;jats:tex-math&gt;$Pr$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;, and identified the scaling of &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:in","PeriodicalId":15853,"journal":{"name":"Journal of Fluid Mechanics","volume":"14 1","pages":""},"PeriodicalIF":3.7,"publicationDate":"2024-08-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142207627","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
Asymptotics of the centre-mode instability in viscoelastic channel flow: with and without inertia 粘弹性通道流中心模式不稳定性的渐近学:有惯性和无惯性
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.500
Rich R. Kerswell, Jacob Page
Motivated by the recent numerical results of Khalid <jats:italic>et al.</jats:italic> (<jats:italic>Phys. Rev. Lett.</jats:italic>, vol. 127, 2021, 134502), we consider the large-Weissenberg-number (<jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline1.png"/> <jats:tex-math>$W$</jats:tex-math> </jats:alternatives> </jats:inline-formula>) asymptotics of the centre mode instability in inertialess viscoelastic channel flow. The instability is of the critical layer type in the distinguished ultra-dilute limit where <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline2.png"/> <jats:tex-math>$W(1-beta )=O(1)$</jats:tex-math> </jats:alternatives> </jats:inline-formula> as <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline3.png"/> <jats:tex-math>$W rightarrow infty$</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="S0022112024005007_inline4.png"/> <jats:tex-math>$beta$</jats:tex-math> </jats:alternatives> </jats:inline-formula> is the ratio of solvent-to-total viscosity). In contrast to centre modes in the Orr–Sommerfeld equation, <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline5.png"/> <jats:tex-math>$1-c=O(1)$</jats:tex-math> </jats:alternatives> </jats:inline-formula> as <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline6.png"/> <jats:tex-math>$W rightarrow infty$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, where <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005007_inline7.png"/> <jats:tex-math>$c$</jats:tex-math> </jats:alternatives> </jats:inline-formula> is the phase speed normalised by the centreline speed as a central ‘outer’ region is always needed to adjust the non-zero cross-stream velocity at the critical layer down to zero at the centreline. The critical layer acts as a pair of intense ‘bellows’ which blows the flow streamlines apart locally and then sucks them back together again. This compression/rarefaction amplifies the streamwise-normal polymer stress which in turn drives the streamwise flow through local polymer stresses at the critical layer. The streamwise flow energises the cross-stream flow via continuity which in turn intensifies the critical layer to close the cycle. We also treat the large-Reynolds-number (<jats:inline-formu
受 Khalid 等人最近的数值结果(《物理评论快报》,第 127 卷,2021 年,134502 期)的启发,我们考虑了无惯性粘弹性通道流中中心模不稳定性的大韦森伯格数($W$)渐近。该不稳定性属于超稀释极限下的临界层类型,当 $W rightarrow infty$ 时,$W(1-beta)=O(1)$ ($beta$ 是溶剂与总粘度之比)。与 Orr-Sommerfeld 方程中的中心模式相反,$1-c=O(1)$为$W rightarrow infty$,其中$c$为按中心线速度归一化的相速度,因为总是需要一个中心 "外部 "区域来调整临界层上的非零横流速度,使其在中心线上降为零。临界层就像一对强烈的 "风箱",将流线局部吹散,然后再将其吸回。这种压缩/还原放大了流向正常聚合物应力,反过来又通过临界层的局部聚合物应力推动流向流动。流向流通过连续性为横向流提供能量,而横向流又反过来加强临界层,从而结束循环。我们还对 $Re$ - $W$ 中性曲线的上分支(其中 $1-c=O(Re^{-2/3}$ )和下分支的大雷诺数($Re$)渐近结构进行了处理,证实了之前数值计算中推断出的标度。最后,我们要指出的是,粘弹性中心模式不稳定性实际上是由 Boffetta 等人首次在粘弹性 Kolmogorov 流动中观察到的(《流体力学》,第 523 卷,2005 年,第 161-170 页)。
{"title":"Asymptotics of the centre-mode instability in viscoelastic channel flow: with and without inertia","authors":"Rich R. Kerswell, Jacob Page","doi":"10.1017/jfm.2024.500","DOIUrl":"https://doi.org/10.1017/jfm.2024.500","url":null,"abstract":"Motivated by the recent numerical results of Khalid &lt;jats:italic&gt;et al.&lt;/jats:italic&gt; (&lt;jats:italic&gt;Phys. Rev. Lett.&lt;/jats:italic&gt;, vol. 127, 2021, 134502), we consider the large-Weissenberg-number (&lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline1.png\"/&gt; &lt;jats:tex-math&gt;$W$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;) asymptotics of the centre mode instability in inertialess viscoelastic channel flow. The instability is of the critical layer type in the distinguished ultra-dilute limit where &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline2.png\"/&gt; &lt;jats:tex-math&gt;$W(1-beta )=O(1)$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; as &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline3.png\"/&gt; &lt;jats:tex-math&gt;$W rightarrow infty$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; (&lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline4.png\"/&gt; &lt;jats:tex-math&gt;$beta$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; is the ratio of solvent-to-total viscosity). In contrast to centre modes in the Orr–Sommerfeld equation, &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline5.png\"/&gt; &lt;jats:tex-math&gt;$1-c=O(1)$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; as &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline6.png\"/&gt; &lt;jats:tex-math&gt;$W rightarrow infty$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt;, where &lt;jats:inline-formula&gt; &lt;jats:alternatives&gt; &lt;jats:inline-graphic xmlns:xlink=\"http://www.w3.org/1999/xlink\" mime-subtype=\"png\" xlink:href=\"S0022112024005007_inline7.png\"/&gt; &lt;jats:tex-math&gt;$c$&lt;/jats:tex-math&gt; &lt;/jats:alternatives&gt; &lt;/jats:inline-formula&gt; is the phase speed normalised by the centreline speed as a central ‘outer’ region is always needed to adjust the non-zero cross-stream velocity at the critical layer down to zero at the centreline. The critical layer acts as a pair of intense ‘bellows’ which blows the flow streamlines apart locally and then sucks them back together again. This compression/rarefaction amplifies the streamwise-normal polymer stress which in turn drives the streamwise flow through local polymer stresses at the critical layer. The streamwise flow energises the cross-stream flow via continuity which in turn intensifies the critical layer to close the cycle. We also treat the large-Reynolds-number (&lt;jats:inline-formu","PeriodicalId":15853,"journal":{"name":"Journal of Fluid Mechanics","volume":"57 1","pages":""},"PeriodicalIF":3.7,"publicationDate":"2024-08-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142207628","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
On the flow dynamics around a surface-mounted cube and boundary layer effects 表面安装立方体周围的流动动力学和边界层效应
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.551
Barbara L. da Silva, David Sumner, Donald J. Bergstrom
Motivated by contradicting or insufficient information regarding the large-scale flow dynamics around surface-mounted finite-height square prisms of small aspect ratio, the present study investigates the dominant vortex shedding and low-frequency dynamics around a surface-mounted cube. These flow modes were obtained from the spectral proper orthogonal decomposition of large-eddy simulation results, at a Reynolds number of $textit {Re}=1times 10^4$ and two different types of boundary layer: a thin and laminar boundary layer with thickness $delta /D=0.2$ and a thick and turbulent boundary layer with $delta /D=0.8$ . The main antisymmetric mode pair revealed a new flow pattern with the alternate shedding of streamwise flow structures, indicating a transition from the half-loops of taller prisms to only streamwise strands (i.e. no vertical core) for smaller aspect ratio. The formation process of the streamwise structures is due to a reorientation of the vorticity of the arch vortex in the streamwise direction characteristic of the shed structures. The low-frequency drift mode affected the length of the recirculation region, the strength of vortex shedding, and the near-wall flow field and pressure distribution on the cube's faces, leading to low-frequency variations in the fluctuating drag and normal force coefficients. These large-scale flow dynamics were similar for both boundary layers, but minor differences were identified, related mostly to the occurrence of flow attachment and the formation of a headband vortex for the thicker boundary layer.
由于有关表面安装的小长宽比有限高度方棱柱周围大尺度流动动力学的信息相互矛盾或不足,本研究对表面安装的立方体周围的主要涡流脱落和低频动力学进行了研究。这些流动模式是在雷诺数为 $textit {Re}=1times 10^4$ 和两种不同类型边界层(厚度为 $delta /D=0.2$ 的薄层流边界层和厚度为 $delta /D=0.8$ 的厚湍流边界层)的条件下,通过对大涡模拟结果进行谱正交分解得到的。主要的反对称模式对揭示了一种新的流动模式,即交替脱落的流向结构,表明在较小的纵横比下,从较高棱柱的半环过渡到只有流向股(即没有垂直核心)。流向结构的形成过程是由于拱形涡旋的涡度在流向方向上的重新定向,这是脱落结构的特征。低频漂移模式影响了再循环区域的长度、涡流脱落的强度以及立方体表面的近壁流场和压力分布,从而导致了阻力和法向力系数的低频波动变化。这两个边界层的大尺度流动动力学相似,但也发现了细微差别,主要涉及较厚边界层的流动附着和头带涡的形成。
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引用次数: 0
Exact coherent structures in two-dimensional turbulence identified with convolutional autoencoders 用卷积自动编码器识别二维湍流中的精确相干结构
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.552
Jacob Page, Joe Holey, Michael P. Brenner, Rich R. Kerswell
Convolutional autoencoders are used to deconstruct the changing dynamics of two-dimensional Kolmogorov flow as <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline1.png"/> <jats:tex-math>$Re$</jats:tex-math> </jats:alternatives> </jats:inline-formula> is increased from weakly chaotic flow at <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline2.png"/> <jats:tex-math>$Re=40$</jats:tex-math> </jats:alternatives> </jats:inline-formula> to a chaotic state dominated by a domain-filling vortex pair at <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline3.png"/> <jats:tex-math>$Re=400$</jats:tex-math> </jats:alternatives> </jats:inline-formula>. ‘Latent Fourier analysis’ (Page <jats:italic>et al.</jats:italic>, <jats:italic>Phys. Rev. Fluids</jats:italic>6, 2021, p. 034402) reveals a detached class of bursting dynamics at <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline4.png"/> <jats:tex-math>$Re=40$</jats:tex-math> </jats:alternatives> </jats:inline-formula> which merge with the low-dissipation dynamics as <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline5.png"/> <jats:tex-math>$Re$</jats:tex-math> </jats:alternatives> </jats:inline-formula> is increased to <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline6.png"/> <jats:tex-math>$100$</jats:tex-math> </jats:alternatives> </jats:inline-formula> and provides an efficient representation within which to find unstable periodic orbits (UPOs) using recurrent flow analysis. Focusing on initial guesses with energy in higher latent Fourier wavenumbers allows a significant number of high-dissipation-rate UPOs associated with the bursting events to be found for the first time. At <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline7.png"/> <jats:tex-math>$Re=400$</jats:tex-math> </jats:alternatives> </jats:inline-formula>, the UPOs discovered at lower <jats:inline-formula> <jats:alternatives> <jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" mime-subtype="png" xlink:href="S0022112024005524_inline8.png"/> <jats:tex-math>$Re$</jats:tex-math> </jats:alternatives> </jats:inline-formula> move away from the attractor, and an entirely different embedding structure is formed within the network devoid of small-scale vortices. Here latent Fourier proje
使用卷积自动编码器解构了二维科尔莫哥罗夫流的动态变化,随着 Re$ 的增加,从 Re=40$ 时的弱混沌流到 Re=400$ 时由域填充漩涡对主导的混沌状态。潜伏傅立叶分析"(Page 等人,Phys. Rev. Fluids6, 2021, p. 034402)揭示了在 $Re=40$ 时与低耗散动力学合并的一类独立的迸发动力学,当 $Re$ 增加到 $100$ 时与低耗散动力学合并。将重点放在具有较高潜伏傅立叶波数能量的初始猜测上,可以首次发现大量与迸发事件相关的高耗散率 UPO。在 $Re=400$ 时,在较低 $Re$ 时发现的 UPO 远离吸引子,网络中形成了完全不同的嵌入结构,没有小尺度涡旋。在这里,潜在傅立叶投影确定了一个相关的 "大尺度 "UPO,我们认为它是欧拉方程解的有限Re$延续。
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引用次数: 0
Collisionless kinetic theory for saltation over a rigid, bumpy bed 刚性凹凸床面盐化的无碰撞动力学理论
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.520
Diego Berzi, Alexandre Valance, James T. Jenkins
We employ the methods of statistical mechanics to obtain closures for the balance equations of momentum and fluctuation kinetic energy that govern the ballistic motion of grains rebounding at a rigid, bumpy bed that are driven by turbulent or non-turbulent shearing fluids, in the absence of mid-trajectory collisions and fluid velocity fluctuations. We obtain semi-analytical solutions for steady and fully developed saltation over horizontal beds for the vertical profiles of particle concentration and stresses and fluid and particle velocities. These compare favourably with measurements in discrete-element numerical simulations in the wide range of conditions of Earth and other planetary environments. The predictions of the particle horizontal mass flux and its scaling with the amount of particles in the system, the properties of the carrier fluid and the intensity of the shearing also agree with numerical simulations and wind-tunnel experiments.
我们采用统计力学方法获得了动量和波动动能平衡方程的闭包,该方程在没有轨迹中段碰撞和流体速度波动的情况下,支配着颗粒在湍流或非湍流剪切流体驱动下在刚性凹凸床面反弹的弹道运动。我们获得了水平床面稳定和完全发展盐化的半解析解,即颗粒浓度和应力以及流体和颗粒速度的垂直剖面。这些结果与在地球和其他行星环境的各种条件下进行的离散元素数值模拟测量结果相比较,效果良好。对颗粒水平质量通量及其与系统中颗粒数量、载流体特性和剪切强度的比例关系的预测也与数值模拟和风洞实验相吻合。
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引用次数: 0
Linear stability of stratified, rotating, viscous plane Couette–Poiseuille flow 分层旋转粘性平面库埃特-普绪耶流的线性稳定性
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.549
William Oxley, Rich R. Kerswell
The linear stability of plane Couette–Poiseuille flow (CPF) is studied with the physical effects of stratification, rotation and viscosity all included for the first time together. With no stratification, two instability mechanisms are present due to the shear and rotation which, for the most part, do not interact as they favour different forms of two-dimensionality. However, there are some small parts of parameter space where new three-dimensional instability appears indicating that Rayleigh's criterion is also violated in parameter space beyond where shear instability is expected. No fully localised centrifugal instabilities can be found for CPF, but they are shown to exist if the base flow shear has a maximum in the domain (the base flow needs to be at least cubic in the cross-stream variable rather than just quadratic as in CPF). With stable stratification present, new instabilities are found due to the combined effects of stratification and rotation, but only some appear to be of the resonance-type associated with the strato-rotational instability. The other unstable branches are more accurately interpreted as a stratification-modified centrifugal instability. Three-dimensional versions of this violate Rayleigh's criterion even when this is extended to include stratification. When stratification is stronger than rotation, the resonance-type instabilities are only dominant for cyclonic flows.
在研究平面库埃特-普瓦耶流(CPF)的线性稳定性时,首次将分层、旋转和粘度的物理效应一并考虑在内。在没有分层的情况下,剪切和旋转会产生两种不稳定机制,而这两种不稳定机制在大多数情况下不会相互作用,因为它们倾向于不同形式的二维性。然而,在参数空间的一些小范围内出现了新的三维不稳定性,这表明在超出预期剪切不稳定性的参数空间内也违反了瑞利准则。在 CPF 中找不到完全局部化的离心不稳定性,但如果基流剪切力在域中达到最大值(基流至少需要是横流变量的三次方,而不是 CPF 中的二次方),则表明离心不稳定性是存在的。在存在稳定分层的情况下,由于分层和旋转的共同作用,发现了新的不稳定现象,但只有部分不稳定现象似乎属于与平流旋转不稳定现象相关的共振型。其他不稳定分支被更准确地解释为分层修正离心不稳定性。这种不稳定的三维版本违反了瑞利准则,即使将其扩展到包括分层。当分层作用强于旋转作用时,共振型不稳定性只在气旋流中占主导地位。
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引用次数: 0
The impact of diffusiophoresis on hydrodynamic dispersion and filtration in porous media 扩散对多孔介质中水动力分散和过滤的影响
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.546
Mamta Jotkar, Pietro de Anna, Marco Dentz, Luis Cueto-Felgueroso
It is known that the dispersion of colloidal particles in porous media is determined by medium structure, pore-scale flow variability and diffusion. However, much less is known about how diffusiophoresis, that is, the motion of colloidal particles along salt gradients, impacts large-scale particle dispersion in porous media. To shed light on this question, we perform detailed pore-scale simulations of fluid flow, solute transport and diffusiophoretic particle transport in a two-dimensional hyper-uniform porous medium. Particles and solute are initially uniformly distributed throughout the medium. The medium is flushed at constant flow rate, and particle breakthrough curves are recorded at the outlet to assess the macroscopic effects of diffusiophoresis. Particle breakthrough curves show non-Fickian behaviour manifested by strong tailing that is controlled by the diffusiophoretic mobility. Although diffusiophoresis is a short-time, microscopic phenomenon owing to the fast attenuation of salt gradients, it governs macroscopic colloid dispersion through the partitioning of particles into transmitting and dead-end pores. We quantify these behaviours by an upscaled analytical model that describes both the retention and release of colloids in dead-end pores and the observed long-time tailings. Our results suggest that diffusiophoresis is an efficient tool to control particle dispersion and filtration through porous media.
众所周知,胶体颗粒在多孔介质中的分散是由介质结构、孔隙尺度流动变化和扩散决定的。然而,人们对扩散oresis(即胶体粒子沿盐梯度的运动)如何影响多孔介质中的大规模粒子分散却知之甚少。为了揭示这个问题,我们对二维超均匀多孔介质中的流体流动、溶质传输和粒子扩散泳移进行了详细的孔隙尺度模拟。粒子和溶质最初均匀分布在整个介质中。以恒定流速冲洗介质,并在出口处记录颗粒突破曲线,以评估扩散泳的宏观效应。粒子突破曲线显示出非费克式行为,表现为受扩散流动性控制的强烈拖尾。尽管由于盐梯度的快速衰减,衍射导流是一种短时间的微观现象,但它通过将颗粒划分为透射孔和末端孔来控制宏观胶体分散。我们通过一个放大的分析模型来量化这些行为,该模型同时描述了胶体在末端孔隙中的滞留和释放以及观察到的长时间尾流。我们的研究结果表明,扩散泳是控制颗粒在多孔介质中的分散和过滤的有效工具。
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引用次数: 0
Low-frequency unsteadiness mechanisms of unstart flow in an inlet with rectangular-to-elliptical shape transition under off-design condition at a Mach number of 4 在马赫数为 4 的非设计条件下,具有矩形到椭圆形过渡形状的进气口中的非启动流动的低频不稳定机制
IF 3.7 2区 工程技术 Q1 MECHANICS Pub Date : 2024-08-22 DOI: 10.1017/jfm.2024.504
Jiaxiang Zhong, Feng Qu, Di Sun, Qingsong Liu, Qing Wang, Junqiang Bai
The unsteady mechanism of unstart flow for an inlet with rectangular-to-elliptical shape transition (REST) under the off-design condition at a Mach of 4 is investigated using the delay detached eddy simulation method. With the help of numerical simulations, the unsteady dynamics, especially the low-frequency characteristics of the REST inlet unstart flow, as well as the self-sustaining mechanism, is investigated. The instantaneous flow illustrates the unsteady phenomena of the REST unstart flow, including the interaction between the cowl-closure leading edge (CLE) shock and the shear layer, breathing of the separation bubble, flapping of the separation shock, instability of the shear layer and vortex shedding along the shear layer. The spectral analysis reveals that the lower frequency dynamics is associated with the breathing of the separation bubble and the flapping motion of the separation shock wave, while the higher frequency is related to the instability of the shear layer affected by cowl-closure leading edge shock and the formation of shedding vortices. Further, coherence analysis shows that the contribution of these flow structures dominating the low-frequency dynamics couple with each other. Based on the dynamic mode decomposition results, the characteristics that contribute to the unsteady behaviour of unstart flow are summarized. The streamwise vortices downstream of the separation and the shedding vortices are believed to be the main driving force of the global low-frequency unsteadiness of the REST inlet unstart flow under the off-design condition. Moreover, the CLE shock plays an important role in the process during the dominant flow structure conversion from the backflow within the separation bubble into elongated streamwise structures.
采用延迟分离涡模拟方法研究了马赫数为 4 的非设计工况下矩形到椭圆形过渡(REST)进气道非启动流的非稳态机理。在数值模拟的帮助下,研究了 REST 入口非启动流的非稳定动力学特性,尤其是低频特性,以及自持机制。瞬时流说明了 REST 非启动流的不稳定现象,包括罩壳前缘(CLE)冲击与剪切层之间的相互作用、分离气泡的呼吸、分离冲击的拍打、剪切层的不稳定以及沿剪切层的涡流脱落。频谱分析表明,低频动力学与分离气泡的呼吸和分离冲击波的拍击运动有关,而高频与受牛顿关闭前缘冲击影响的剪切层的不稳定性和脱落涡的形成有关。此外,相干性分析表明,这些主导低频动力学的流动结构的贡献相互耦合。根据动力学模式分解结果,总结了导致非起始流不稳定行为的特征。在非设计条件下,分离下游的流向涡和脱落涡被认为是 REST 入口非启动流全局低频不稳定性的主要驱动力。此外,在主要流动结构从分离气泡内的回流转化为细长流向结构的过程中,CLE 冲击也发挥了重要作用。
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引用次数: 0
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Journal of Fluid Mechanics
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