Local phase holdups in an inverse three-phase turbulent bed of 150 mm i.d. and 4350 mm height were measured simultaneously by micro-electrical conductivity probe technique in this study.The experiments were carried ou...Local phase holdups in an inverse three-phase turbulent bed of 150 mm i.d. and 4350 mm height were measured simultaneously by micro-electrical conductivity probe technique in this study.The experiments were carried out with polyethylene particles （dp=4.01 mm, ρs=926 kg·m -3）,air, and water[0.05%（mass）SCMC, 0.20%（mass）SCMC] as solid phase,gas phase and liquid phase respectively.540 sets of experimental data of local phase holdups in radial direction were obtained under Ug=U g3. It was found that the distribution of local solid holdup showed a maximum peak at r/R=（0.75—0.90）. The range of maximum peaks was larger than that of conventional fluidized beds. The distribution of local gas holdup in radial direction showed a maximum value at the column center and a minimum value near the wall.Moreover,the non-homogeneous distribution of local gas holdup in radial directions was more evident than that of conventional fluidized beds.The different operation regimes as well as the corresponding three specific gas velocities （U g1 ,U g2 and U g3） were obtained on the basis of the axial distribution characteristics of cross-sectional average solid holdups.The effect of the operating conditions （liquid viscosity, initial volume fraction of solids H s0/H0, initial liquid height H l0 ） on the specific gas velocities was presented.展开更多
利用前人所提出的对应态基团贡献法(Corresponding State Group Contribution,简称CSGC),回归了包括烷烃、烯烃、炔烃、酮、酯、萘、环氧化合物、含磷化合物、含硫、含氮、含硅等20类291种纯物质(共2,042个数据点)在不同温度下的液体黏...利用前人所提出的对应态基团贡献法(Corresponding State Group Contribution,简称CSGC),回归了包括烷烃、烯烃、炔烃、酮、酯、萘、环氧化合物、含磷化合物、含硫、含氮、含硅等20类291种纯物质(共2,042个数据点)在不同温度下的液体黏度值,得到94个基团对临界温度和临界压力的贡献值以及方程的11个模型参数,总平均相对误差为6.13%.并且用10种未参与回归的物质(共79个数据点)对方程进行了验证,平均误差为67.9%.展开更多
文摘Local phase holdups in an inverse three-phase turbulent bed of 150 mm i.d. and 4350 mm height were measured simultaneously by micro-electrical conductivity probe technique in this study.The experiments were carried out with polyethylene particles （dp=4.01 mm, ρs=926 kg·m -3）,air, and water[0.05%（mass）SCMC, 0.20%（mass）SCMC] as solid phase,gas phase and liquid phase respectively.540 sets of experimental data of local phase holdups in radial direction were obtained under Ug=U g3. It was found that the distribution of local solid holdup showed a maximum peak at r/R=（0.75—0.90）. The range of maximum peaks was larger than that of conventional fluidized beds. The distribution of local gas holdup in radial direction showed a maximum value at the column center and a minimum value near the wall.Moreover,the non-homogeneous distribution of local gas holdup in radial directions was more evident than that of conventional fluidized beds.The different operation regimes as well as the corresponding three specific gas velocities （U g1 ,U g2 and U g3） were obtained on the basis of the axial distribution characteristics of cross-sectional average solid holdups.The effect of the operating conditions （liquid viscosity, initial volume fraction of solids H s0/H0, initial liquid height H l0 ） on the specific gas velocities was presented.
文摘利用前人所提出的对应态基团贡献法(Corresponding State Group Contribution,简称CSGC),回归了包括烷烃、烯烃、炔烃、酮、酯、萘、环氧化合物、含磷化合物、含硫、含氮、含硅等20类291种纯物质(共2,042个数据点)在不同温度下的液体黏度值,得到94个基团对临界温度和临界压力的贡献值以及方程的11个模型参数,总平均相对误差为6.13%.并且用10种未参与回归的物质(共79个数据点)对方程进行了验证,平均误差为67.9%.
