共查询到20条相似文献,搜索用时 125 毫秒
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讨论了平均二相流基本方程的封闭问题。在此基础上 ,从建立数学模型的角度 ,提出将水利工程中的水气二相流划分为稀疏气泡流区、气相连续流区和掺气形成区 (稠密气泡流 )三个区 ;根据已有的方程封闭的研究成果 ,提出了可用于稀疏气泡流计算的双流体模型。 相似文献
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Fluent软件是用于模拟和分析在复杂几何区域内的流体流动与热交换问题的专用CFD软件。将k-e模型与多相流技术Mixture模型相结合,借助Fluent软件进行多相流分析,对喷嘴处的气穴流场进行了数值模拟,并计算了模型内二维轴对称气穴流场的液态水的体积分数分布及压力分布。 相似文献
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多维喷雾两相流模型的计算和验证 总被引:2,自引:2,他引:0
本文提出了一个反映瞬态喷雾两相作用主要因素的二维轴对称喷雾两相流模型。文章讨论了模型的主要假设,给出了计算公式和离散化方法。文章中所提供的计算示例以及试验对照证明了模型的可行性和实用性。 相似文献
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柴油机热态喷雾二维两相流模型研究 总被引:1,自引:0,他引:1
摘要本文提出了一个柴油机热态喷雾二维两相流理论模型.模型强调了液滴的湍流扩散、高压蒸发特征以及与气相场的强烈耦合作用.给出了根据该理论模型所编制的TDSP软件的部分计算结果,并就这些结果进行了分析讨论. 相似文献
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采用一阶和修正二阶的滑移连续介质模型,对跨努森数区域的低速微通道流进行二维和三维数值模拟。用实验结果和DSMC方法验证滑移连续介质模型在跨努森数区域中的适用性,并详细讨论了微通道流的可压缩效应、稀薄效应、低雷诺数效应和三维特性。研究表明,努森数是表征稀薄效应和模型适用性的特征参数,滑移连续介质模型适用于努森数小于0.150的氮气流动;马赫数不再是微通道流可压缩效应的唯一标识参数;雷诺数是表征低雷诺数效应和三维特性的关键参数,高宽比大于20的微通道流具备良好的二维特性。 相似文献
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本文运用离散相模型和多孔介质模型建立了柴油机颗粒捕集器的二维物理模型和气固两相流模型.研究表明模拟的多孔介质流场压力与实验测量结果相对误差小于±5%,模拟的颗粒捕集率达到75%~92%,且与流速和颗粒直径有关,研究结果对颗粒捕集器的优化设计提供了依据. 相似文献
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流化床内气固两相流动一直是实验研究和数值模拟的热点。基于Eulerian双流体模型,本文建立了流化床内的气固两相流动模型,采用FLUENT软件对流化床密相区两相流动特性、床内气泡的产生运动和爆裂等特性进行了数值模拟。模型中,将颗粒相看作是连续介质,建立与气相相同形式的数学模型;采用了离散介质动力理论,引入颗粒温度来描述固相粘性应力,并用气固曳力进行气固两相耦合。模拟得到了气泡产生、运动和爆裂的变化过程,与实验结果相一致。采用不同的曳力模型对流化床稠密两相流动进行了模拟,与Kuipers实验对比,结果表明采用Gidaspow曳力模型描述流化床稠密两相流动特性更准确。 相似文献
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考虑壁面粗糙度的双流体颗粒-壁面碰撞模型 总被引:3,自引:1,他引:3
提出了考虑壁面粗糙度的双流体颗粒-壁面碰撞模型,将轨道模型中颗粒碰壁模型考虑壁面粗糙度和双流体模型中用概率密度函数积分法处理颗粒与光滑壁面碰撞模型的优点结合起来,引入壁面粗糙度对碰壁颗粒湍流影响的机理。数值模拟结果表明,由于考虑了各方面雷诺应力之间的相互转化,雷诺应力从平均运动中得到能量,以及壁面对运动的衰减作用等因素,包括摩擦系数、恢复系统、壁面粗糙度等物理参数的颗粒-壁面碰撞模型作为边界条件时,得到的结果与实验符合得更好。 相似文献
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Shi LIU Runsheng YAN Haigang WANG Fan JIANG Xiangyun DONG Institute of Engineering Thermophysics Chinese Academy of Sciences P.O. Box Beijing China 《热科学学报(英文版)》2004,13(2):179-186
The successful application of Electrical Capacitance Tomography (ECT) depends heavily on the image reconstruction speed and quality. The two requirements usually cannot be satisfied simultaneously. Also, for a large number of acquired 2D ECT images, a 3D presentation of them is much desired to track the variations of the material distribution in a third dimension. To facilitate ECT for practical flow analyses in process engineering, the authors have recently developed algorithms for 3D image presentation and for online iterative image reconstruction that only takes the same time as a linear back projection method but yields good image qualities as the Landweber iterative method does. The new methods have been successfully applied to visualize several classes of two phase flows, namely fluidization, cyclone separation, circulating rate determination in circulating fluidized beds, pneumatic conveying, rotating drum mixing. Special characteristics in each case have been discussed and valuable results are obtained, which are reported in this paper. 相似文献
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A four-equation model is proposed for prediction of dilute turbulent gas-solid flows where the ratio of the particle and the gas densities is large. The model is based on explicit algebraic relations for Reynolds stresses and turbulent fluxes of the void fraction, which were derived in an earlier work within the context of Reynolds-averaged Navier-Stokes (RANS) methodology. These relations are manipulated here to derive nonlinear eddy-viscosity-type models for thin-shear flows. Further, new models are proposed for third-order correlations which are also simplified for thin-shear flows. These models are used to propose four transport equations for the turbulence kinetic energy of the carrier phase and its rate of dissipation, the turbulence kinetic energy of the dispersed phase, and the velocity covariance of the two phases. The final four-equation model is implemented for prediction of a particle-laden turbulent jet, and encouraging agreements with available laboratory data are observed. 相似文献
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A scalar fluctuation model for two phase flows is proposed for RANS (Reynolds Average Navier Stokes) simulations. It is a two equation model based on the variance v of the gaseous fuel mass fraction and on the scalar dissipation χ. For each quantity a transport equation is solved. The models developed by Mantel and Borghi [11] and Newman et al. [9] are used to close the transport equation of χ for gaseous flows. These models (and an algebraic closure for χ) are compared to (Direct Numerical Simulation) DNS results obtained by Eswaran and Pope [12] in the case of mixing in a gaseous homogeneous stationary turbulence. To get a correct agreement between the RANS models and the DNS results, we had to adjust some constants in these models. It is shown that with the algebraic model it is not possible to correctly reproduce the trends observed in the DNS. Then, the closure proposed by Demoulin and Borghi [13] for the spray source term in the variance equation is adopted. The modelling of the spray source term in the scalar dissipation equation represents the main theoretical work of this paper. Comparisons between experiments and computations are performed in order to validate the complete model. These comparisons are performed on a Gasoline Direct Injection optical access engine. To make comparisons between computations and experiments possible, it is necessary to filter the computed variance. This procedure allows to account for the filtering performed by the pixels of the CCD camera used in the experiments. The two- equation models of Newman et al. and Mantel and Borghi used with the variance and scalar dissipation source terms proposed in this paper predict a high turbulence to mixing time ratio r=τtτm=χυ?k during the evaporation of droplets. This high mixing rate allows the model of Newman et al. to correctly reproduce fluctuation levels in the spark zone as well as the intense fluctuation in the spray region, while the model of Mantel and Borghi tends to over-estimate fluctuation levels. On the contrary, the algebraic closure imposes a fixed ratio r of the order of 2, which leads to a very high over-prediction of fluctuation levels. These results show that a two-equation model with appropriate spray source terms is needed for correctly modeling the mixing in two-phase flows. 相似文献