共查询到18条相似文献,搜索用时 951 毫秒
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局部热壁面多孔介质方腔内自然对流的数值研究 总被引:1,自引:0,他引:1
本文对上下壁面绝热、左侧壁面长度为b的嵌装加热器部分维持恒定温度T_h而剩余部分绝热,且右侧壁面维持恒定温度T_c的多孔介质方腔内的自然对流换热进行了数值研究.在热壁面无量纲长度B=0.5(B=b/L)的条件下,综合研究了左侧壁面受热部分中心距上壁面的无量纲长度D(D=d/L)、Da数、Ra数和孔隙率对腔体内自然对流换热的影响.数值计算结果表明,左侧壁面受热部分位置的不同对腔体内自然对流换热有很大的影响,D在0.6附近取值时,Na数最大.Da数、Ra数对腔体的自然对流换热影响较大,而孔隙率对换热的影响较小. 相似文献
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为研究不连续冷源边界对内置发热体多孔介质方腔内传热及流动的影响,采用格子Boltzmann方法对REV尺度下多孔介质方腔内的自然对流进行计算,并研究瑞利数(Ra)、达西数(Da)、孔隙度对多孔介质方腔内传热流动的影响.发现Da对方腔内的流体流型影响很大,Da为10-4时,多孔介质方腔内只有一个涡流,而Da为10-2时,方腔内有两个涡流.增大Ra、Da、孔隙度可以提高冷源壁面的平均努赛尔数(Nu),增强散热效果,孔隙率对平均Nu影响程度和Da的大小有关.当冷源布置在壁面上方,壁面的平均Nu随Ra的增加剧烈变化,方腔处于高Ra条件下时,将冷源布置在边界的上方可以提高散热效果.6种布置方案中Case 6的散热效果最好. 相似文献
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复合方腔顶盖驱动双扩散混合对流格子Boltzmann模拟 总被引:1,自引:0,他引:1
《工程热物理学报》2017,(3)
为本文基于热质耦合的Lattice Bhatnagar-Gross-Krook(CLBGK)模型,通过引入浓度分布函数,利用格子Boltzmann方法对顶盖驱动的复合方腔内的双扩散混合对流现象进行了研究,复合方腔由多孔介质区域和自由空间组成。分析了路易斯数Le=2.0,浮升力比N=1.0,格拉晓夫数Gr=10~4和普朗特数Pr=0.7时,孔隙率(ε=0.6/0.7/0.8)、方腔中多孔介质层位置及理查德森数Ri(10~(-3)≤Ri≤10~3)对内部混合对流及热质扩散的影响。给出了方腔内温度、浓度和流线分布,以及高温高浓度壁面的平均努塞尔数Nu_(av)和平均舍伍德数Sh_(av)。研究结果表明:多孔介质层对顶盖驱动方腔内热质双扩散影响显著,且方腔左壁壁面平均努塞尔数Nu_(av)与平均舍伍德数Sh_(av),在位置D_1~D_3之间随多孔介质层的右移而增大,在位置D_3上随Ri(10~(-3)≤Ri≤10~3)的增大而减小。 相似文献
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《物理学报》2020,(16)
利用格子玻尔兹曼方法 (lattice Boltzmann method, LBM) 对倾斜多孔介质方腔内 Al_2O_3-H_2O 纳米流体的自然对流进行数值模拟, 考虑了孔隙率 (0.3 ≤?≤ 0.9)、瑞利数 (10~3 ≤ Ra ≤ 10~6)、纳米颗粒体积分数(0 ≤ ? ≤ 0.04) 和倾斜角 (0°≤γ≤ 120°) 等因素的影响, 研究了正弦温度分布边界条件下倾斜多孔介质方腔内纳米流体的自然对流传热机理. 结果表明: 若?和γ保持不变时, 随着 Ra 数的增大, 热壁面处的平均努塞尔数 (Nu_(ave) 数) 呈现出先减小后增大的趋势; 对于给定的 Ra 数, 当γ = 0°时, 随着孔隙率的增大, 热壁面处Nu_(ave) 数逐渐增大, 当γ = 40°, 80°和 120°时, Nuave 数在?= 0.7 左右时达到最大值; 若?和 Ra 数保持不变, 当γ = 40°时, 方腔内的自然对流换热效率最强, 当γ = 80°时热壁面自然对流换热效率被削弱. 最后, 研究了纳米颗粒体积份数的影响, 当方腔施加一定倾角时, 热壁面处的 Nuave 数随着纳米颗粒体积分数的增大而增大. 相似文献
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对三维多孔介质倾斜方腔内非稳态自然对流换热进行数值研究.腔体右壁面(X=1)保持恒温T0,左壁面(X=0)基于温度T0按正弦规律变化,其他所有壁面保持绝热.采用Brinkman扩展达西模型及SIMPLE算法模拟方腔内的流动.方腔沿y轴转动倾角α1的变化范围为0°~90°,沿x轴转动倾角α2的变化范围为0°~45°,无量纲温度震荡频率f的变化范围为5π~90π.详细研究倾角和温度震荡频率对三维方腔自然对流换热的影响.计算结果表明:当倾角α1=46°,α2=45°及温度震荡频率f=45π时,方腔内的换热最强. 相似文献
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采用Boltzmann方法模拟部分热活跃边界下的多孔腔体内自然对流,探讨不同热边界布置方案、孔隙度、Da数及Ra数对其流动传热的影响.数值计算表明:Da=10-4时,腔体内中央出现一个循环流模式,只在Ra数很大时孔隙度才对传热有影响; Da=10-2时,腔体内出现两个循环流,在Ra数很小时孔隙度对传热产生强烈的的影响.热活跃边界位置影响腔体内流体对流传热的强度,加热边界布置在底部、而冷却边界布置在顶部(Bottom-Top布置方式),对多孔腔体内对流传热最有利,优于全热边界布置方式的传热效果. 相似文献
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小液滴撞击壁面现象在喷雾冷却等领域都有广泛应用.为研究小液滴(微米)撞击热壁面(非沸腾区)传热过程,建立了二维液滴撞壁瞬态模型,并采用相场方法对小液滴换热过程中对流热通量和导热热通量的大小进行了对比.研究结果表明:液滴撞击壁面初期形成“冷斑”,有利于小液滴与壁面的传热;小液滴撞击壁面过程中热通量峰值存在于三相接触点附近,数量级在105—106 W/m2;小液滴撞击壁面过程中受壁面浸润性和液滴尺寸对传导热通量的影响较为显著,而速度和液滴尺寸对对流热通量的影响较为显著;大多数情况下,小液滴撞击壁面传导热通量数量级在103—105 W/m2,对流热通量数量级在104—106 W/m2,对流热通量大于传导热通量,在整个换热过程中占据主导地位. 相似文献
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利用CFD软件数值研究了颗粒三维有序堆积多孔介质的对流换热问题. 采用颗粒直径分别为14 mm,9.4 mm和7 mm的球形颗粒有序排列构成多孔介质骨架,在多孔骨架的上方有一恒热流密度的铜板. 采用流固耦合的方法研究了槽通道内温度分布和局部对流换热系数的分布以及对流换热的影响因素. 研究结果表明:热渗透的厚度和温度边界层的厚度在流动方向上逐渐增大,并且随流量的增加而减小;当骨架的导热系数比较高时,对流换热随颗粒直径的减小而略有增大;对流换热系数随聚丙烯酰胺溶液浓度的增大而减小,黏性耗散减弱了对流换热.
关键词:
多孔介质
温度场
局部对流换热系数
数值模拟 相似文献
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采用格子Boltzmann方法对可变形腔体内自然对流问题进行数值研究,给出平均努赛尔数的经验关系式.腔体左壁加热长度分为左壁面的整个区域(H)和左壁面的中间区域(0.5H)两种情况,右壁向外界环境开放,上下边界绝热且可以上下移动,以此调节右出口尺寸.主要研究瑞利数(104 ≤ Ra ≤ 106),右出口尺寸(1.0H ≤ L ≤ 2.0H),左壁加热尺寸(Lh=0.5H或Lh=H)对腔体内等温线、流线、局部努塞尔数和平均努赛尔数的影响.结果表明:腔体内换热随着瑞利数的增大越来越强烈,表现为椭圆形准静止区域更加靠近上绝热壁,且热分层厚度逐渐变小,平均努赛尔数增加.而右出口尺寸的增加,对于两种加热尺寸下腔内的换热效果有不同程度影响,其中与加热尺寸为左壁面的全部区域Lh=H相比,加热尺寸为左壁面的中间情况Lh=0.5H时,右侧开口尺寸的增加对换热效果的影响不显著.此外,左壁加热尺寸为0.5H时显示出比加热尺寸为H时更高的平均传热效率.最后,针对不同的加热尺寸,提出加热面平均努赛尔数与Ra数及右壁面开口尺寸L*之间函数关系的经验预测,拟合效果满足工程实践与设计需要. 相似文献
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A.M. Rashad T. Armaghani A.J. Chamkha M.A. Mansour 《Chinese Journal of Physics (Taipei)》2018,56(1):193-211
The effects of a heat sink and the source size and location on the entropy generation, MHD natural convection flow and heat transfer in an inclined porous enclosure filled with a Cu-water nanofluid are investigated numerically. A uniform heat source is located in a part of the bottom wall, and a part of the upper wall of the enclosure is maintained at a cooled temperature, while the remaining parts of these two walls are thermally insulated. Both the left and right walls of the enclosure are considered to be adiabatic. The thermal conductivity and the dynamic viscosity of the nanofluid are represented by different verified experimental correlations that are suitable for each type of nanoparticle. The finite difference methodology is used to solve the dimensionless partial differential equations governing the problem. A comparison with previously published works is performed, and the results show a very good agreement. The results indicate that the Nusselt number decreases via increasing the nanofluid volume fraction as well as the Hartmann number. The best location and size of the heat sink and the heat source considering the thermal performance criteria and magnetic effects are found to be D?=?0.7 and B?=?0.2. The entropy generation, thermal performance criteria and the natural heat transfer of the nanofluid for different sizes and locations of the heat sink and source and for various volume fractions of nanoparticles are also investigated and discussed. 相似文献
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采用格子Boltzmann方法研究填充水-氧化铝纳米流体的等腰直角三角形腔体中的自然对流。讨论瑞利数、颗粒体积分数、热源位置等因素对对流换热的影响,以及不同纳米流体模型对模拟结果的影响。结果表明:在低瑞利数下,随着热源在左壁面向上移动,换热效率逐渐增加。而在高瑞利数(Ra=106)时,观察到相反的现象;采用单相纳米流体模型,模拟表明热壁面平均努塞尔数比率随着体积分数的增加近似线性增加。采用改进的纳米流体模型,结果显示平均努塞尔数比率随着体积分数的增加而增大,但是平均努塞尔数比率的变化斜率逐渐减小。改进模型模拟的换热效率比单相模型高,这是因为改进模型考虑了粒子间作用力及换热,更符合实际情况。 相似文献
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Thermo-Solutal Natural Convection in an Anisotropic Porous Enclosure Due to Non-Uniform Temperature and Concentration at Bottom Wall 下载免费PDF全文
Ashok Kumar Pravez Alam & Prachi Fartyal 《advances in applied mathematics and mechanics.》2015,7(5):644-662
This article summaries a numerical study of thermo-solutal natural convection
in a square cavity filled with anisotropic porous medium. The side walls of the
cavity are maintained at constant temperatures and concentrations, whereas bottom
wall is a function of non-uniform (sinusoidal) temperature and concentration. The
non-Darcy Brinkmann model is considered. The governing equations are solved numerically
by spectral element method using the vorticity-stream-function approach.
The controlling parameters for present study are Darcy number $(Da)$, heat source intensity
i.e., thermal Rayleigh number $(Ra)$, permeability ratio $(K^∗)$, orientation angle $(ϕ)$. The main attention is given to understand the impact of anisotropy parameters
on average rates of heat transfer (bottom, $Nu_b$, side $Nu_s$) and mass transfer (bottom, $Sh_b$, side, $Sh_s$) as well as on streamlines, isotherms and iso-concentration. Numerical
results show that, for irrespective value of $K^∗$, the heat and mass transfer rates are negligible
for $10^{-7}≤Da≤10^{−5}, Ra=2×10^5$ and $ϕ=45^◦$. However, a significant impact
appears on Nusselt and Sherwood numbers when Da lies between $10^{−5}$ to $10^{−4}$. The
maximum bottom heat and mass transfer rates ($Nu_b, Su_b$) is attained at $ϕ=45^◦$, when $K^∗= $0.5 and 2.0. Furthermore, both heat and mass transfer rates increase on increasing
Rayleigh number ($Ra$) for all the values of $K^∗$. Overall, It is concluded from the above
study that due to anisotropic permeability the flow dynamics becomes complex. 相似文献
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Natural convection heat transfer in the presence of a magnetic field has received considerable attention in the past few decades because of its various applications in industrial installations. In particular, a large number of numerical studies analyzing the effect of the magnetic field on natural convection in a two-dimensional cavity have been performed. In this work, we propose to study the main characteristics of the convective heat transfer of pure fluids and nanofluids in a two-dimensional cavity differentially heated and subjected to an external magnetic field. The scale analysis method is used first to obtain a correlation giving the heat transfer rate, which is then developed to predict the behavior of the heat transfer rate for pure fluids and nanofluids. To verify the reliability of the theoretical predictions, a numerical study is also carried out. The results show that the proposed correlation predicts well the convective heat transfer characteristics obtained numerically. 相似文献