共查询到19条相似文献,搜索用时 842 毫秒
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本文对以带钢连续热镀锌为背景抽象出的锌锅中低Pr流体的流动和传热进行了数值模拟.数值结果显示,对Re=0的纯自然对流,Ra在104和105间时数值解由稳态解分岔为振荡解;对于Ra=0的纯强制对流,Re在4×103和5x1003之间时,数值解从稳态解分岔为振荡解;当Ra和Re均小于自然对流和强制对流单一机制作用时发生振荡的临界值时,混合对流的流动和传热为稳态;当Ra和Re中的一个参数大于单一机制作用发生振荡的临界值时,另一个参数由小于增加到大于单一机制作用发生振荡的临界值时,数值解由振荡解变为稳态解. 相似文献
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采用SIMPLE算法,QUICK差分格式,对底部加热三维长方体腔内空气的自然对流进行了数值模拟。根据模拟结果,探讨了方腔内流体流动与换热的静态分岔与振荡等非线性现象。数值结果显示,在固定的几何尺寸和不同Ra的情况下,当初始场不同时,会出现若干不同的解,即存在解的静态分岔;在固定的几何尺寸和相同的初始场情况下,低Ra时流动和换热处于稳态,当Ra超过某一临界值时,流动和换热就会随时间振荡,并通过倍周期分岔过渡到混沌;当方腔的几何尺寸不同时,分岔点的特征值Ra也发生变化。 相似文献
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封闭圆内开缝圆自然对流换热的振荡特性 总被引:1,自引:0,他引:1
本文通过数值计算探讨了封闭圆内开缝圆自然对流换热的振荡特性。数值计算以整个圆为计算区域,采用了非稳态的数学模型和具有QUICK差分格式的SIMPLE算法。在相同条件下计算结果和实验结果符合很好。数值结果显示, 当几何结构一定时,Rayleigh数Ra小于某个临界值时,流动和换热处于稳态,并且关于垂直中心线对称;Ra大于这个临界值时,流动和换热是振荡的,非对称的。数值实验还表明,流动和换热出现振荡时的临界Rayleigh数Rac与开缝圆的开缝度有关,且流动和换热的振荡会出现对称振荡和非对称振荡两种情形。 相似文献
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Mixed convection in an open cavity with a heated wall bounded by a horizontally unheated plate is investigated experimentally. The cavity has the heated wall on the inflow side. Mixed convection fluid flow and heat transfer within the cavity is governed by the buoyancy parameter, Richardson number (Ri), and Reynolds number (Re). The results are reported in terms of wall temperature profiles of the heated wall and flow visualization for Re = 100 and 1000, Ri in the range 30–110 (for Re = 1000) and 2800–8700 (for Re = 100), the ratio of the length to the height of cavity (L/D) is in the range 0.5–1.5, and the ratio of the channel height to cavity height (H/D) is in the range of 0.5 and 1.0. The present results show that the maximum dimensional temperature rise values decrease as the Reynolds and the Richardson numbers decrease. The flow visualization points out that for Re = 1000 there are two nearly distinct fluid motions: a parallel forced flow in the channel and a recirculation flow inside the cavity. For Re = 100 the effect of a stronger buoyancy determines a penetration of thermal plume from the heated plate wall into the upper channel. Nusselt numbers increase when L/D increase in the considered range of Richardson numbers. 相似文献
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The paper represents results on numerical investigation of flow and heat transfer between two isothermal vertical plates under laminar natural convection. A system of complete Navier–Stokes equations is solved for a two-dimensional gas flow between the plates along with additional rectangular regions (connected to inlet and outlet sections), whose characteristic sizes are much greater than the spacing between the plates. The calculations were performed over very wide ranges of Rayleigh number Ra = 10 ÷ 105 and a relative channel length AR = L/w = 1 ÷ 500. The influence of the input parameters on the gas-dynamic and thermal structure of thermogravitational convection, the local and mean heat transfer, and also the gas flow rate between the plates (convective draft. We determined sizes of the regions and regime parameters when the local heat flux on the walls tends to zero due to the gas temperature approach to the surface temperature. It is shown that the mean heat transfer decreases as the relative channel length AR grows, whereas the integral gas flow rate (convective draft) and Reynolds number in the channel Re = 2wUm/ν increase. The use of a modified Rayleigh number Ra* = Ra · (w/L) (Elenbaas number) leads to generalization of calculation data on mean heat transfer. These data are in good agreement with the correlations for heat transfer [1, 2] and gas flow rate [3]. The reasons of variation of the data in the range of low Rayleigh numbers are discussed in detail. 相似文献
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The present study investigated fluid flow and natural convection heat transfer in an enclosure embedded with isothermal cylinder. The purpose was to simulate the three-dimensional natural convection by thermal lattice Boltzmann method based on the D3Q19 model. The effects of suspended nanoparticles on the fluid flow and heat transfer analysis have been investigated for different parameters such as particle volume fraction, particle diameters, and geometry aspect ratio. It is seen that flow behaviors and the average rate of heat transfer in terms of the Nusselt number (Nu) are effectively changed with different controlling parameters such as particle volume fraction (5 % ≤ φ ≤ 10 %), particle diameter (d p = 10 nm to 30 nm) and aspect ratio (0.5 ≤ AR ≤ 2) with fixed Rayleigh number, Ra = 105. The present results give a good approximation for choosing an effective parameter to design a thermal system. 相似文献
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竖直圆管中超临界压力CO2对流换热实验研究 总被引:5,自引:1,他引:4
本文对超临界压力CO2在竖直加热圆管内的对流换热进行了实验研究,比较了不同流向、不同热流密度等对流动和换热的影响。实验结果表明,管内径为2mm时,在低进口Re条件下,由于浮升力影响导致层流向湍流提前转变, 对流换热增强;与向上流动相比,向下流动更易由层流转变为湍流;向下流动的换热要强于向上流动,表明浮升力对换热有很大影响。对于管内径为0.27 mm的微细圆管,当进口Re高于104时,浮升力的影响可以忽略,对流换热系数的变化完全由物性的变化尤其是cp的变化导致。 相似文献
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Space-averaged surface temperature distributions and overall Nusselt number measurements have been carried out to study the transient mixed convection heat transfer in a channel with two facing and symmetrically heated semicircular cavities. Effects of buoyancy, channel orientation, and channel aspect ratio on thermal behavior have been investigated from Re 500 to 1,500. Depending on the parametric set, steady, oscillatory, and irregular thermal regimes have been identified. The natural frequencies and time scales of the oscillatory regimes have been obtained using spectral analysis. Results show that with increase in channel aspect ratio, the heat transfer performance reduces for all inclination angles. 相似文献
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对非牛顿流体在小尺寸方形通道内的低雷诺数受迫对流传热进行了实验研究。实验用介质为1500wppmCarbopol-934中性水溶液。通道顶壁受到等热流加热。结果表明,流体粘弹性与传热的相互作用取决于雷诺数的大小。当表观雷诺数Re>11.5时,非牛顿流体开始强化对流传热。Re数越高,传热强化的程度越大。流体的阻力系数则几乎不受粘弹性的影响。 相似文献
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The natural convection flow phenomena that occur inside an enclosed space are very interesting examples of complex fluid systems
that may yield to analytical, empirical and numerical solutions, and many reports have looked into this basic problem. In
the present study, heat transfer and fluid flow for natural convection in a horizontal rectangular container with a free surface
are investigated using infrared thermography. The temperature field was measured and visualized at a gas-liquid (air — silicon
oil) interface using infrared thermography. The heat transfer phenomena were also investigated by statistically analyzing
the temperature data. The applicability of the infrared thermography to quantitative heat transfer measurement at the gas-liquid
interface was evaluated. It is revealed that infrared thermography is effective not only in visualization of a gas-liquid
interface but also in heat transfer measurement. A new heat transfer correlation is proposed for the gas-liquid interface
of this flow system. The coefficient of heat transfer can be summarized by a specific heat transfer correlation formula regardless
of several conditions, including container aspect ratio, fluid viscosity and fluid layer depth. 相似文献
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b/a=0.5的椭圆形通道内非牛顿流体的强化传热 总被引:1,自引:0,他引:1
对非牛顿流体在小尺寸椭圆形通道内的层流受迫对流传热进行了实验研究。实验介质为1500Wppm的Carbopol-934中性水溶液。采用直接通电的方法对管壁四周等热流加热。结果表明,椭圆通道内,非牛顿流体Carbopol水溶液的换热强于牛顿流体水,约高出水50%左右,说明粘弹性流体在椭圆形通道内也产生二次流并能强化换热;与同种浓度的Carbopol水溶液在方形通道内的换热结果相比,椭圆通道内的换热高于方形通道。流体的压力降则不受粘弹性的影响,仍符合幂律流体的阻力系数关系式(f=16/Re*)。 相似文献