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首页> 外文期刊>International Journal of Heat and Fluid Flow >Gas-liquid slug flow in a horizontal concentric annulus, a comparison of numerical simulations and experimental data
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Gas-liquid slug flow in a horizontal concentric annulus, a comparison of numerical simulations and experimental data

机译:气液块在水平同心环中流动,数值模拟和实验数据的比较

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Multiphase flow simulations were run in OpenFOAM utilizing InterFoam, a volume of fluid type solver. A concentric annulus geometry was constructed and periodic boundary conditions were applied to alleviate the requirement for a longer domain. The simulations were run in 3, 5 and 7 m long domains with the annulus dimensioned such that the outer and inner cylinder diameter were 0.1 and 0.05 m respectively. The 4 individual mesh designs were constructed such that the coarsest mesh consists of 102k cells/m while the finest mesh was generated with 400k cells/m. Each mesh was significantly refined within 0.005 m of both the inner and outer cylinder wall. The simulation data was compared with experimental pressure and holdup data collected at Institute for Energy Technology in Norway. The 3 and 7 m domains reproduced slug frequencies to within 9% of the experiment results of 1.43 Hz for all mesh densities. Comparatively, the 5 m domain has larger errors with respect to slugging frequency (22-27%). The 5 m case performs poorly, probably due to an artificial restraint introduced by the limitation of available liquid which is set as alpha(oil) = 0.53 for all cases. The alpha(oil) restriction combined with the domain length determines the amount of liquid in the system. This interaction of factors means that the domain length is an important parameter when preparing the simulation. The pressure data display a stronger dependence on the mesh quality in comparison to the slug frequency analysis. The 3 m domain with a 400k cells/m mesh resulted in a maximum and minimum pressure gradient of 1783.5 and 803.9 Pa/m, compared to the experiment values of 1785 and 822 Pa/m, which are within 3% of the expected results.
机译:利用互换的OpenFoam运行多相流动模拟,一定体积的流体型求解器。构建同心环形几何形状,并施加周期性边界条件以减轻更长域的要求。仿真在3,5和7米长的域中运行,其尺寸为尺寸,使得外部和内筒直径分别为0.1和0.05米。构造了4个单独的网状设计,使得粗元件由102K电池/ m组成,而使用400K单元/ m生成最佳网格。每个网格在内外圆筒壁的0.005米中显着精制。将模拟数据与挪威能源技术研究所收集的实验压力和持有数据进行了比较。 3和7 M个结构域将SLUX频率转换为对所有网眼密度的1.43Hz的实验结果的9%内。相比之下,5米域对振荡频率(22-27%)具有更大的误差。 5米的情况表现不佳,可能是由于在所有案例中设定为α(油)= 0.53的可用液体引入的人为约束。与畴长结合的α(油)限制决定了系统中的液体量。这种因素的相互作用意味着域长度是准备模拟时的重要参数。与SLUI频率分析相比,压力数据显示对网格质量的更强依赖性。与400K细胞/ m网的3M域导致最大和最小压力梯度为1783.5和803.9 pa / m,与1785和822 pa / m的实验值相比,这在预期结果的3%范围内。

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