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The explicit compact difference scheme, proposed in Three-point explicit compact difference scheme with arbitrary order of accuracy and its application in CFD by Lin et al., published in Applied Mathematics and Mechanics (English Edition), 2007, 28(7), 943-953, has the same performance as the conventional finite difference schemes. It is just another expression of the conventional finite difference schemes. The proposed expression does not have the advantages of a compact difference scheme. Nonetheless, we can more easily obtain and implement compared with the conventional expression in which the coefficients can only be obtained by solving equations, especially for higher accurate schemes. 相似文献
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To predict the characteristics of dense liquid-solid two-phase flow, K-ε-T model is established, in which the turbulent flow of fluid phase is described with fluid turbulent kinetic energy Kf and its dissipation rate εf, and the particles random motion is described with particle turbulent energy Kp and its dissipation rate εp and pseudothermal temperature Tp. The governing equations are also derived. With K-ε-T model, numerical study of dense liquid-solid two-phase turbulent up-flow in a pipe is performed. The calculated results are in good agreement with experimental data of Alajbegovic et al. (1994), and some flow features are captured. 相似文献
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基于Ca(OH)2/CaO的热化学储能体系在实验中均表现出孔隙结构的显著变化,而该现象在已有的大多数数值模拟研究中并未被考虑。本文针对该现象建立了变孔隙率反应动力学模型及非稳态“流动–传热–化学反应”耦合模型,并基于此对直接、间接传热式固定床反应器中Ca(OH)2/CaO的定/变孔隙率脱水反应过程特征参数(反应渗透率、压力、温度、反应速率及转化率等)变化进行了对比模拟研究。结果表明:定孔隙率模型与变孔隙率模型之间有明显的差异,且变孔隙率模型更能体现实际反应过程的特征。以初始孔隙率为0.8的工况为例,定孔隙率假设在直接传热式反应器中的转化速率比变孔隙率模型快19.8%,而在间接传热式反应器中转化速率比变孔隙率慢6.1%。说明以往研究中使用的定孔隙率假设高估了直接传热式反应器的性能,而低估了间接传热式反应器的性能。 相似文献
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本文将“米”字形放射状槽道强化面积大、气泡脱离阻力小与毛细芯成核位点多等优点相结合,设计加工出一系列铜基放射状槽道与烧结毛细芯耦合散热表面,在10 K、20 K和30 K三个不同过冷度下进行了HFE-7100池沸腾换热实验,得到不同表面在不同过冷度条件下的沸腾换热性能。结果表明,槽深对换热影响较大,耦合毛细芯的铜基散热结构可以进一步提高临界热流密度和换热系数。最大临界热流密度和换热系数分别可达130.1 W/cm2和0.94 W/(cm2·K),并对实验过程中的气泡动力学行为进行了分析。 相似文献