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SIMULTANEOUS CONTROL OF FRICTION DRAG REDUCTION AND HEAT TRANSFER AUGMENTATION BY TRAVELING WAVE-LIKE BLOWING/SUCTION 通过行波式吹风/吸力同时控制摩擦阻力减少和传热增加
IF 1.5 Q2 Mathematics Pub Date : 2011-12-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011003213
K. Higashi, H. Mamori, K. Fukagata
The possibility of simultaneous control for skin-friction drag reduction and heat transfer augmentation by a traveling wave-like blowing/suction is explored for a laminar channel flow. In addition to the constant temperature difference condition, uniform heat generation is considered for the temperature field so that the boundary condition similar to that for the velocity field holds. Friction drag reduction and heat transfer augmentation are simultaneously achieved when the wave travels in the upstream direction. The global phases of streamwise velocity and temperature fluctuations are found to oppose each other, which eventually leads to dissimilarity between the friction drag and heat transfer. Direct numerical simulation (DNS) confirms that this dissimilar control effect can also be obtained in a turbulent channel flow.
探讨了在层流通道中通过行波式吹吸同时控制表面摩擦阻力减小和传热增强的可能性。在考虑等温差条件的基础上,对温度场考虑均匀产热,使其符合与速度场相似的边界条件。当波浪在上游方向传播时,同时实现了摩擦阻力的减少和传热的增加。发现沿流速度和温度波动的全局相位是相反的,这最终导致了摩擦阻力和换热之间的不一致。直接数值模拟(DNS)证实了这种不同的控制效果也可以在湍流通道流动中获得。
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引用次数: 11
Effects of buoyancy on the performance of a vertical double-pipe heat exchanger 浮力对立式双管换热器性能的影响
IF 1.5 Q2 Mathematics Pub Date : 2011-01-21 DOI: 10.1615/COMPUTTHERMALSCIEN.2011003483
I. Voicu, N. Galanis, T. Maré
CFD simulations of heat transfer between two fluids in a parallel-flow vertical double-pipe heat exchanger, taking into consideration conduction in the walls, viscous dissipation, variable fluid properties, and axial diffusion in the fluids, illustrate the effects of buoyancy on the velocity and temperature profiles as well as on the Nusselt numbers and friction coefficients. In particular, the results show that flow reversal occurs at different positions depending on the flow direction. In the developing region, the fluid bulk temperatures, the wall temperature, and the local Nusselt numbers for both fluids depend on the flow direction. For the conditions under consideration, the Nusselt number for the fully developed flow in the inner pipe lies between the corresponding forced convection values for the constant heat flux and constant temperature conditions, while the one in the annulus is smaller than both these forced convection values. It is established that the flow and thermal fields in the inner cylinder and the annulus cannot be predicted correctly by studying each one separately since the thermal condition at the solid wall separating the two fluids depends on flow characteristics such as the Richardson number in the inner tube.
考虑壁面传导、粘性耗散、变流体性质和流体的轴向扩散等因素,对平行流垂直双管换热器中两种流体之间的换热进行CFD模拟,说明浮力对速度和温度分布以及努塞尔数和摩擦系数的影响。结果表明,流动方向不同,在不同位置会发生回流。在发展区,两种流体的体积温度、壁面温度和局部努塞尔数都依赖于流动方向。在所考虑的条件下,管内充分流动的努塞尔数介于恒热流密度和恒温条件下对应的强制对流值之间,而环空的努塞尔数小于这两种强制对流值。由于分离两种流体的固体壁面的热状况取决于内管内Richardson数等流动特性,因此不能通过单独研究来准确预测内筒和环空的流动和热场。
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引用次数: 1
MIXED CONVECTION-RADIATION HEAT TRANSFER IN A VENTED PARTITIONED RECTANGULAR ENCLOSURE 矩形通风隔离罩内对流-辐射混合传热
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011002585
A. Bahlaoui, A. Raji, M. Hasnaoui, M. Naïmi
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引用次数: 0
INFLUENCE OF BOILER SWING RATE ON DYNAMICS OF THERMAL AND FLOW CHARACTERISTICS IN WATER CIRCULATION BOILERS 锅炉摆频对水循环锅炉热流动力学特性的影响
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2012004188
M. Habib, I. Al-Zaharnah, T. Ayinde, S. Al-Anizi, Y. Al-Awwad
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引用次数: 3
NUMERICAL STUDY OF A TRANSITIONAL NATURAL VENTILATION FLOW DRIVEN BY A LINE SOURCE PLUME WITH VARIED REYNOLDS AND PRANDTL NUMBERS 变雷诺数和普朗特数线源羽流驱动的过渡自然通风流的数值研究
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011003212
T. Hattori, S. Armfield, M. Kirkpatrick, S. Maruyama, A. Komiya
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引用次数: 2
COMBINED EFFECTS OF RADIATION AND NATURAL CONVECTION IN A SQUARE CAVITY SUBMITTED TO CROSS GRADIENTS OF TEMPERATURE: CASE OF PARTIAL HEATING AND COOLING 受温度梯度影响的方形腔内辐射和自然对流的联合效应:局部加热和局部冷却的情况
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.V3.I1.60
R. El Ayachi, A. Raji, M. Hasnaoui, A. Abdelbaki, Mohamed Naimi
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引用次数: 3
EFFECT OF GAS RADIATION AND LAMINAR FORCED CONVECTION ON EVAPORATION 气体辐射和层流强迫对流对蒸发的影响
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011003070
F. B. Nejma, K. Slimi
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引用次数: 2
HEAT AND MASS TRANSFER CONTROL BY EVAPORATIVE THERMAL PATTERNING OF THIN LIQUID LAYERS 通过薄液体层的蒸发热模式控制传热传质
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011003229
C. Iorio, O. Goncharova, O. Kabov
For several years, interfacial instabilities arising in evaporating layers of volatile liquid when subjected to a shear flow of inert and non-absorptive gas have been studied for their intrinsic complexity due to the interaction between different phenomena such as heat and mass transfer through the layer interface, thermo-capillarity, natural convection, and shear-induced stresses. More recently, the possibility of generating ordered thermal patterns in an evaporating layer by controlling such kinds of instabilities has been considered as an intriguing technique to enhance heat and mass transfer in precisely defined spots at the interface of the layers. We studied numerically the topology of the thermal patterns as well as the heat and mass transfer characteristics that can be induced in an evaporating liquid layer by controlling the thickness of the layer while keeping constant the gas flow intensity. Calculations have been conducted by considering ethanol as the working fluid and nitrogen as the inert gas. The thickness of the layer was varied in order to have aspect ratios with respect to the characteristic length of the evaporating interface in the range of 0.02-1. The inspiring reason for performing the simulations reported in this paper is the preparation of the CIMEX-1 experiment that will be performed on-board the International Space Station in the next future. For that reason, all the calculations presented refer to the condition of the absence of gravity. © 2011 by Begell House, Inc.
多年来,人们一直在研究挥发性液体蒸发层在受到惰性和非吸收性气体剪切流动时产生的界面不稳定性,因为它们的内在复杂性是由于不同现象之间的相互作用,如通过层界面的传热传质、热毛细作用、自然对流和剪切诱导应力。最近,通过控制这种不稳定性在蒸发层中产生有序热模式的可能性被认为是一种有趣的技术,可以在层的界面上精确定义的点上增强传热和传质。本文通过数值模拟研究了在一定气体流动强度的情况下,控制蒸发液层厚度所产生的热模式拓扑结构和传热传质特性。以乙醇为工质,氮气为惰性气体进行了计算。为了使蒸发界面特征长度的纵横比在0.02-1范围内,改变了层的厚度。执行本文中报道的模拟的鼓舞人心的原因是准备CIMEX-1实验,该实验将在未来的国际空间站上进行。因此,所有的计算都是在没有重力的情况下进行的。©2011 by Begell House, Inc。
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引用次数: 39
Performance comparison of relations for nanofluids properties in the CFD prediction of mixed convection 混合对流CFD预测中纳米流体性质关系的性能比较
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.2011002831
M. Akbari, N. Galanis, A. Behzadmehr
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引用次数: 0
LIQUID FILMS FALLING ON HORIZONTAL PLAIN CYLINDERS: PART 1-EXPERIMENTAL AND NUMERICAL STUDY OF FLOW BEHAVIOR 落在水平平面圆柱体上的液膜:第1部分-流动特性的实验和数值研究
IF 1.5 Q2 Mathematics Pub Date : 2011-01-01 DOI: 10.1615/COMPUTTHERMALSCIEN.V3.I2.60
F. Jafar, G. Thorpe, O. Turan
In this paper, an experimental and numerical investigation of liquid film falling over three horizontal plain cylinders is presented. The flow Reynolds number range studied is 50−2000, rendering the flow laminar. Numerical predictions are obtained using FLUENT, a proprietary computational fluid dynamic (CFD) code, for the 2D and 3D configurations of the three cylinders. In the numerical predictions, the mathematical approach is based on the volume of fluid (VOF) method to account for the fluid's two phases, namely, air and water. The primary objective of the present study was to carry out experiments to validate the numerical code. It was found that increasing the Reynolds number resulted in the flow mode changing from droplet, to jet, to sheet mode. The numerical analyses accurately predicted the Reynolds numbers at which these transitions occur. The flow mode is also related to the separation distance between the horizontal cylinders. The flow mode tends to be droplet at large separation, whereas it tends to be jet and sheet modes at small separations. The distances between adjacent columns of droplets and the adjacent jet decrease with increasing Reynolds number and cylinder diameter, a phenomenon also captured by the numerical analyses. No effects of hysteresis were observed on the spacing of the columns of droplets and jets as the Reynolds number was increased and decreased. The frequency at which droplets fell from all of the cylinders increased when the distance between the water feeder and the cylinder increased, and this effect exhibited hysteresis as the flow rate was successively increased and decreased.
本文对液膜在三个水平平面圆柱体上的下落进行了实验和数值研究。所研究的流动雷诺数范围为50 ~ 2000,呈现层流状态。使用FLUENT(一种专有的计算流体动力学(CFD)代码)对三个圆柱体的二维和三维结构进行了数值预测。在数值预测中,数学方法是基于流体体积(VOF)方法来考虑流体的两相,即空气和水。本研究的主要目的是进行实验来验证数值代码。结果表明,雷诺数的增加导致了流态由液滴流态、射流流态、片状流态转变。数值分析准确地预测了发生这些转变的雷诺数。流动方式也与水平气缸之间的分离距离有关。在大的分离条件下,流动模式倾向于液滴,而在小的分离条件下,流动模式倾向于射流和片状。随着雷诺数的增加和圆柱直径的增大,相邻的液滴柱与相邻的射流柱之间的距离减小,数值分析也捕捉到了这一现象。随着雷诺数的增大和减小,液滴和射流柱间距不受迟滞的影响。随着给水机与筒体距离的增加,各个筒体滴下的频率增加,且随着流量的先后增大和减小,滴下频率表现出滞后性。
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引用次数: 3
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Computational Thermal Sciences
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