کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
238669 | 465768 | 2009 | 11 صفحه PDF | دانلود رایگان |
In this work, the Eulerian–Eulerian multiphase model is used in the computational simulation of fluid dynamics of spouted beds with two different geometries: conical–cylindrical and conical. For the conical–cylindrical spouted bed, the simulated results of radial velocities of particles with a 1.41 mm diameter along bed heights in the range of 0.022 to 0.318 m are compared with experimental values obtained by He et al. [Y.L. He, C.J. Lim, J.R. Grace and, J.X. Zhu, Measurements of Voidage Profiles in Spouted Beds, Canadian Journal of Chemical Engineering, 72 (1994), 229–234], and show a good agreement. The influence of static bed height on the characteristic curve is assessed through simulations using different airflow rates. The respective minimum spouting velocities are compared with experimental values and with values obtained through empirical correlations reported in the literature. The results of the CFD simulations show a deviation of 3.8% when compared with the experimental data, which is less than the aforementioned correlations. The stages of transition from the condition of static bed to spouting bed are presented through the simulation of solids volume fraction distribution and the radial profile of voidage in the spouting region. The characteristic curve and minimum spouting conditions for a simulated conical bed, with glass particles of 6 mm diameter are compared with the experimental results showing deviations of 12.1% for the pressure drop and 5.6% for the minimum spouting velocity.
In this work, the Eulerian-Eulerian multiphase model is used to simulate two geometries of spouted bed: conical-cylindrical and conical. The minimum spouting velocities are compared with experimental values and with values from empirical correlations. The stages of transition from static bed to spouting bed are presented through the simulation of solids volume fraction distribution and the radial profile of voidage.Figure optionsDownload as PowerPoint slide
Journal: Powder Technology - Volume 188, Issue 3, 10 January 2009, Pages 195–205