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21.
Asymmetric horizontal thermal profiles can change the flow field structure in the physical vapor transport (PVT)of Hg2Cl2. It is found that for the ratios of horizontal to vertical thermal Rayleigh numbers RaH/Ra ≥ 1·5, the convetive flow structure changes from multicellular to unicellular for the base parametric state of Ra = 2·79 × 104, Pr = 0·91, Le=l·01. Pe = 4·60, Ar= 0·2 and Cr = 1·01. The unicellular flow structure obtained by increasing ∇*H(RaH) is not likely to support the conjecture of the presence of unicellular convective mode in the laser Doppler velocimetry (LDV) experiments for PVT process of Hg2Cl2 (Kim el al., 1996). When the six parameters of Ra, Pr, Le, Pe, Ar and Cr are fixed, the dimensional maximum magnitude of the velocity vector |U|max is proportional to √∇T*H. 相似文献
22.
The inverse problem approach by conjugate gradient with adjoint equations is adapted to the context of a non-isothermal bioprocess, controlled by internal heat generation from microbial oxidation, as could be found in a composting reactor for instance, to determine the heat source from internal temperature measurements. The volumetric heat source is assumed proportional to the rate of consumption of a substrate by a biomass, as described by a Monod model. Computations are performed for Rayleigh numbers equal to 0.25 and 25, for a representative biochemical reaction under typical boundary conditions, for constant and temperature-dependent model parameters. The influence of noisy input data is also considered. It is found that good solutions can be obtained when heat release and diffusion occur over very different time scales. The variation of the model parameters with temperature must be taken into account, but single sensor solutions are possible at relatively small Rayleigh numbers when convection is present. 相似文献
23.
Boundary layer equations for free convection heat transfer along a semi-infinite horizontal plate are derived by giving more importance to the energy equation. The equations are obtained for low Prandtl number and two separate polynomials are used to approximate the temperature and velocity profiles in these regions. The rate of heat transfer is compared with the available analytical and numerical results based on conventional boundary layer equations. 相似文献
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25.
A numerical study is presented for magnetohydrodynamic free convection of an electrically conducting fluid in a shallow cavity heated from below and cooled from above. The side walls are maintained adiabatic. A uniform magnetic field, inclined with an angle 0 with respect to the horizontal plane, is externally imposed. The investigation covers the range of the Rayleigh number, Ra, from 1.8 × 103 to 3 x 104the Hartmann number, Ha, from 0 to 35, the Prandtl number, Pr, from 0.005 to 1 and aspect ratio of the cavity, A = 6. The effect of the magnetic field on the flow structure is presented. For supercritical convection it is found that, upon increasing Ha, the number of roll cells in the cavity increases when it is perpendicular to it. The imposition of an inclined magnetic field gives rise to new flow patterns with tilted lateral cell walls. The effect of both strength and orientation of the magnetic field on the overall heat transfer is found to be significant. 相似文献
26.
Wei-Mon Yan 《加拿大化工杂志》1993,71(1):54-62
Numerical results are presented for effects of latent heat transport associated with film vaporization on laminar mixed convection heat and mass transfer in a vertical channel with a half channel width b = 0.01 m. The influences of the inlet liquid mass flowrate and wall temperature on the film vaporization and the associated heat and mass transfer characteristics are examined for air-water and air-ethanol systems with gas Reynolds number Reg = 2000. Predicted results obtained by including transport in the liquid film are contrasted with those where liquid film transport is neglected, showing that the assumption of an extremely thin film made in Lin et al. (1988) and Yan and Lin (1989) is only valid for systems having small liquid mass flow rates. Additionally, it is found that the interfacial heat flux is predominantly determined by latent heat transfer connected with film evaporation. 相似文献
27.
采用非稳态数学模型对突扩通道内横掠圆管流动与换热进行了数值模拟。分别对不同雷诺数Re以及不同通道突扩比Er情况进行数值模拟。结果表明:随着Re的变化,数值解有稳态,周期振荡和混沌。同时随着雷诺数的增加,圆管附近的换热不断增强。对于不同突扩比,当10≤Re≤100和250≤Re≤300时,圆管的换热随着通道突扩比的增加而变弱;当100Re≤200时,圆管换热并不单调减弱。 相似文献
28.
加热面边界条件对MEB形成过程的影响 总被引:1,自引:0,他引:1
为研究加热面周围边界条件对气泡微细化沸腾的影响,结合实验与数值模拟对加热面低于水箱底面0.5 mm以及与之齐平两种条件下加热面上气泡行为和气泡周围流场进行对比分析。实验结果表明,50 K过冷度下,加热面齐平时,会发生旺盛的MEB现象,而对于加热面下沉时,微细化沸腾现象不发生。数值分析表明,加热面下沉时,气泡周围Marangoni对流被减弱,且气泡顶部的冷凝被大幅削减。这使得气泡稳定地在加热面上形成并逐渐长大,无法形成微细化沸腾现象。因此,气膜周围的Marangoni对流和气液界面上的冷凝过程可能是导致微细化沸腾发生的主要原因。 相似文献
29.
在菲克定律与质量守恒定律的基础上建立了模拟云南核桃干燥过程的一维非稳态传质数学模型.通过边界条件的处理,结合云南核桃热风干燥试验,对其干燥过程中内部各层水分分布进行了模拟预测.将含水率的预测值与试验值对比可知该模型与试验数据吻合得很好,试验条件下云南核桃的有效水分扩散系数变化范围为1.14×10-9~1.73×10-9 m2/s.干燥初期云南核桃表层的含水率下降速度比内层快得多,之后内层含水率下降速度比表层要快,最终各层含水率稳步下降;从表层到中心,湿度梯度随着干燥时间的增加逐渐减小.分析表明在核桃的干燥过程中,外壳是影响水分扩散的主要阻力之一.该模型有助于云南核桃干燥过程传热传质耦合的研究以及复杂模型的建立. 相似文献
30.
为理论上有效预测超声作用对污泥对流干燥过程的影响,基于非平衡热力学理论,建立了超声场作用下污泥对流干燥热湿耦合迁移过程的数学模型.对不同声能密度作用下污泥内部温度及湿度场分布进行数值模拟.结果表明,超声作用可以有效加速污泥内部的湿迁移过程,但超声强化效果随污泥厚度增大而逐渐减弱.此外,超声热效应使污泥温度有所升高,但污泥内部的温度梯度却略有降低,因此,污泥内部由温度梯度引起的湿分扩散并未因超声波作用而得到强化. 相似文献