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采用边界相似解对恒热流竖壁下降液膜发展中的层流流动与换热特性进行了分析,获得了发展段长度,液膜厚度和无量纲换热系数的计算表达式。 相似文献
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《节能》2017,(6):19-24
为了深入探究水平管降膜蒸发的微观传热特性,采用基于VOF法的计算流体模型对水平管外降膜蒸发进行数值模拟,通过求解控制方程得到液膜内的温度场和速度场。分析了不同入口边界温度和Re数下管外薄液膜内热边界层、无量纲温度和局部传热系数的微观传热特性变化规律,定量给出了热发展区与充分热发展区的边界位置。模拟结果表明:液膜入口温度越高,液膜热发展区覆盖的圆周角度越小;液膜内的热发展区覆盖的角度随Re数的增大而增加是平均传热系数随Re数增大的原因;管外圆周方向无量纲温度分布证明了液膜中的传热包含导热和对流传热;管外液膜内纯导热系数与局部传热系数的差值随倾斜角的增加而减少是由于对流效应沿管圆周方向减弱引起的。 相似文献
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采用修正的膜模型与Nusselt凝结理论结合的方法,对含湿混合气体自上而下横掠水平管外时的对流冷凝换热机理进行研究,建立了液膜流动和传热模型,进行数值求解并分析了雷诺数、壁面温度及水蒸汽浓度等因素对混合气体冷凝换热的影响。计算结果表明:水管外壁液膜厚度分布很大程度上受气体边界层对液膜剪切力的影响。而局部努谢尔数不同于纯蒸气的的冷凝换热,它受气相热阻的影响很大,其分布状况类似于单相气体管外的对流换热。 相似文献
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建立了竖直壁面降膜流动的二维几何模型,运用VOF方法对雷诺数200~1 000的降膜的波动特性进行了数值模拟。研究了液膜的波动特征、液膜流动方向的速度变化以及液体雷诺数对液膜波动的影响规律。结果表明:根据液膜的形态可以将流动区域分为入口区、发展区和稳定区三部分。入口区的液膜相对比较平滑,发展区的液膜表现为频率较高的小幅波动,稳定区的液膜波动幅度增加而频率减小;入口区的最大流速大于初始流速,发展区的最大流速在初始流速上下波动,而稳定区流速小于初始流速;随着液体雷诺数的增加,液膜厚度增加而波幅降低。 相似文献
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《International Communications in Heat and Mass Transfer》2006,33(7):917-927
An analysis has been developed for studying the evaporative cooling of liquid film falling inside a vertical insulated tube in turbulent gas stream is presented. Heat and mass transfer characteristics in air–water system are mainly considered. A low Reynolds number turbulence model of Launder and Sharma is used to simulate the turbulent gas stream and a modified Van Driest model suggested by Yih and Liu is adopted to simulate the turbulent liquid film. The model predictions are first compared with available experimental data for the purpose of validating the model. Parametric computations were performed to investigate the effects of Reynolds number, inlet liquid temperature and inlet liquid mass flow rate on the liquid film cooling mechanism. Results show that significant liquid cooling results for the system with a higher gas flow Reynolds number Re, a lower liquid flow rate Γ0 or a higher inlet liquid temperature TL0. 相似文献
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ABSTRACTIn this paper, a new two-dimensional simulation model was developed for the falling film flow under low Reynolds number (below 20). The phase-field multiphase lattice Boltzmann model was developed to simulate the flow pattern of the two-phase falling film with high density ratio. The approaches to treating the liquid-gas interface with high density ratio (up to 775), surface tension, gravity, inlet and outlet open boundary conditions as well as solid-liquid interface considering contact angle were developed firstly, and then implemented in the model. The dynamic characteristics of the film flow, including the development of the liquid-gas interface and the film thickness, were simulated under the Reynolds numbers between 1.0 and 20. The results show that the film is fully laminar under low Reynolds numbers. The falling film flow model developed in this study lays the foundation for the study of heat and mass transfer in the falling film based liquid desiccant dehumidifier. 相似文献
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Asim Mukhopadhyay Anandamoy Mukhopadhyay 《International Journal of Heat and Mass Transfer》2009,52(3-4):709-715
Weakly nonlinear stability analysis of a thin liquid film falling down a heated inclined plane with linear temperature variation in the presence of a uniform normal electric field has been investigated within the finite amplitude regime. A generalized kinematic equation for the development of free surface is derived by using long wave expansion method. A normal mode approach and the method of multiple scales are used to investigate the linear and weakly nonlinear stability analysis of film flow, respectively. It is found that both Marangoni and electric Weber numbers have destabilizing effect on the film flow. The study reveals that both supercritical stability and subcritical instability are possible for this type of film flow. It is interesting to note that both the Marangoni and electric Weber numbers have qualitatively same influence on the stability characteristics but the effect of Marangoni number is much stronger compare to the electric Weber number. Scrutinizing the effect of Marangoni and electric Weber numbers on the amplitude and speed of waves it is found that, in the supercritical region amplitude and speed of the nonlinear waves increases with the increase in Marangoni and electric Weber numbers, while in the subcritical region the threshold amplitude decreases with the increase in Marangoni and electric Weber numbers. Finally, we obtain that spatially uniform solution is side-band stable in the supercritical region for our considered parameter range. 相似文献
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Chii-Dong Ho Hsuan Chang Hsi-Jen Chen Cheng-Liang Chang Hsieh-Hsung Li Yin-Yu Chang 《International Journal of Heat and Mass Transfer》2011,54(15-16):3740-3748
Falling film microreactors, which provide very high specific interfacial area, have become a promising solution to the fast and strongly exothermic/endothermic gas–liquid reaction systems. A computational fluid dynamic simulation of the two-phase flow for a falling film microreactor is presented using the volume of fluid (VOF) model. The hydrodynamic characteristics, from both 2-D and 3-D simulations, including liquid film thickness, velocity, pressure and shear stress profiles, are analyzed. 2-D simulation is adopted for the study of the relationship of liquid flow rate and film thickness, as well as the effects of gas flow rate, surface tension, liquid viscosity and pressure difference on the liquid flow rate. 3-D simulation is necessary to provide the comprehensive flow profiles. Although the system is in the laminar flow regime, the liquid film features a wavy structure and the velocity profiles are complex. 相似文献
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Yuanyuan Zhou Jianlin Yu Yanzhong Li 《International Journal of Heat and Mass Transfer》2012,55(23-24):7218-7222
In this study, a mathematical model for the laminar falling film is presented in order to simulate the evaporation heat transfer characteristics in falling liquid oxygen films. The model takes into account the effect of the interfacial shear. The values of the film thickness, the heat transfer coefficient as well as the interfacial shear are obtained under given conditions by solving the model with an iteration method. The influences of the inlet Reynolds number, channel length and the interfacial shear on the flow and heat transfer characteristics of the falling film evaporation are analyzed in detail. Effects of key factors on the circulation ratio of the inlet fluid mass flow rate to the generated vapor mass flow rate, an important design parameter for reboilers/condensers, are particularly analyzed. In addition, the variations of the average vapor velocity and interfacial film velocity are also discussed. The analysis results could provide theoretical guidance for the simulation and design of downflow reboilers/condensers applied in air separation units. 相似文献
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Wastewater treatment is one of the most effective solutions to manage the problem of water scarcity. Falling film evaporators are excellent technology in wastewater treatment plants. These wastewater evaporators provide high heat transfer, short residence time in the heating zone, and high-purity distilled water. In the present study, the mechanism of turbulent falling film evaporation in a vertical tube has been investigated. A model has been developed for symmetrical two-dimensional pure and saline water flow in a vertical tube under constant wall heat flux. The numerical simulation has been carried out by a commercial computational fluid dynamics code. The evaporation of saturated liquid film is simulated utilizing a two-phase volume of fluid method and Tanasawa phase-change model. The main objective of this study is to evaluate the effects of water salinity, liquid Reynolds number, wall heat flux, and liquid film thickness on the two-phase heat transfer coefficient and vapor volume fraction. The numerical heat transfer coefficients are compared with the obtained results by Chen's empirical correlation. With a MAPE ≤ 11%, this study proves that the numerical method is highly effective at predicting the heat transfer coefficient. Moreover, the empirical coefficient of the Tanasawa model and the minimum thickness of the falling film are determined. 相似文献