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A STUDY OF STEADY HEATED TWO-PHASE FLOW IN VERTICAL ROUND TUBES.

机译:垂直圆管中稳态加热的两相流动的研究。

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Various literature models of flow regimes and transitions are contrasted and compared to reported observations. The annular flow regime is modelled by average velocities and distributions of the three "fluids"--liquid film, drops and vapor--in the radial and circumferential directions. Accurate empirical correlations giving rates of interfluid mass and momentum transfer are found to be crucial in predicting the location of tube wall dryout.; A possible direct effect of the heat flux on the droplet entrainment rate is hypothesized. Physically the model involves bubble nucleation at the heated tube wall, migration through the turbulent film and rupture at the film-vapor interface accompanied by a spattering of droplets. From considerations of the energies of the surging liquid jet following the bubble rupture, as well as the bubble size and density, the rate of liquid mass entrainment is predicted.; Since in several industrial applications the heat flux results from light originating at a single azimuth, a model to calculate the transmitted fraction of this radiation is developed. A finite element analysis of heat conduction within the tube cross-section is utilized. Boundary conditions include the incident heat flux profile and wall temperature dependent radiative and convective losses at the outer tube surface, as well as nucleative and convective heat transfer at the liquid-coated inner surface.; Finally a computer code is written to compare predictions of the above models to experimental data available in the literature. The accuracy of the heat flux induced entrainment model could not be determined from the burnout data since large amounts of error in the empirical deposition rate correlations cloud the effect. However the pipe conduction model was evaluated independently by simulation of solar boiler tests in which the overall heat flux, entrainment and deposition rates were low. Predictions of the inner and outer wall temperatures at the most strongly heated azimuth were fairly good, with discrepancies explained by the omission of circumferential variations in film thickness and velocity in the fluid flow model.
机译:对比各种流态和过渡的文献模型,并将其与已报道的观测结果进行比较。环形流动状态是通过径向和圆周方向上的三个“流体”(液膜,液滴和蒸汽)的平均速度和分布来建模的。准确的经验相关性给出了流体间质量和动量传递的速率,对于预测管壁变干的位置至关重要。假设热通量可能对液滴的夹带率有直接影响。从物理上讲,该模型包括在加热管壁上产生气泡成核,通过湍流膜迁移并在膜-蒸汽界面破裂,并伴随液滴的飞溅。考虑到气泡破裂后涌动的液体射流的能量,以及气泡的大小和密度,可以预测液体质量的夹带速率。由于在一些工业应用中,热通量是由源自单个方位角的光产生的,因此开发了一种计算该辐射的透射比的模型。利用管横截面内的热传导的有限元分析。边界条件包括在外管表面的入射热通量分布和与壁温有关的辐射和对流损耗,以及在液体涂层内表面处的成核和对流传热。最后,编写计算机代码以将上述模型的预测与文献中提供的实验数据进行比较。无法从燃尽数据确定热通量诱导的夹带模型的准确性,因为经验沉积速率相关性中的大量误差会影响效果。然而,通过模拟整体热通量,夹带和沉积速率较低的太阳能锅炉测试,可以独立地评估管道传导模型。对最强加热方位角的内壁和外壁温度的预测是相当不错的,其差异可以通过在流体流动模型中省略膜厚度和速度的周向变化来解释。

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