针对风力机叶片结冰问题,采用欧拉两相流模型和FLUENT用户自定义函数(user defined function,UDF)计算NACA64618翼型/叶片的水滴收集系数。结果表明:水滴主要撞击在翼型前缘小范围内。随着攻角增大,水滴撞击极限往翼型压力面移动。受三...针对风力机叶片结冰问题,采用欧拉两相流模型和FLUENT用户自定义函数(user defined function,UDF)计算NACA64618翼型/叶片的水滴收集系数。结果表明:水滴主要撞击在翼型前缘小范围内。随着攻角增大,水滴撞击极限往翼型压力面移动。受三维效应的影响,叶尖区域水滴收集系数急剧减小,减小量最大可达59.6%。展开更多
Based on Fluent software,the gas−liquid two-phase flow in the horizontal stirred tank was simulated with SST k−ωturbulence model,Eulerian−Eulerian two-fluid model,and multi-reference flame method.The mixing process i...Based on Fluent software,the gas−liquid two-phase flow in the horizontal stirred tank was simulated with SST k−ωturbulence model,Eulerian−Eulerian two-fluid model,and multi-reference flame method.The mixing process in the tank was calculated by tracer method.The results show that increasing the rotating speed or gas flow is conducive to a more uniform distribution of the gas phase and accelerates the mixing of the liquid phase.When the rotating speed exceeds 93 r/min,the relative power demand remains basically constant.The change in the inclination angle of the upper impeller has minimal effect on the gas phase distribution.When the inclination angle is 50°,the relative power demand reaches the maximum.An appropriate increase in the impeller distance from the bottom improves the gas holdup and gas phase distribution but increases the liquid phase mixing time.展开更多
文摘针对风力机叶片结冰问题,采用欧拉两相流模型和FLUENT用户自定义函数(user defined function,UDF)计算NACA64618翼型/叶片的水滴收集系数。结果表明:水滴主要撞击在翼型前缘小范围内。随着攻角增大,水滴撞击极限往翼型压力面移动。受三维效应的影响,叶尖区域水滴收集系数急剧减小,减小量最大可达59.6%。
基金financially supported by the Fundamental Research Funds for the Central Universities of Central South University,China(No.2020zzts515)。
文摘Based on Fluent software,the gas−liquid two-phase flow in the horizontal stirred tank was simulated with SST k−ωturbulence model,Eulerian−Eulerian two-fluid model,and multi-reference flame method.The mixing process in the tank was calculated by tracer method.The results show that increasing the rotating speed or gas flow is conducive to a more uniform distribution of the gas phase and accelerates the mixing of the liquid phase.When the rotating speed exceeds 93 r/min,the relative power demand remains basically constant.The change in the inclination angle of the upper impeller has minimal effect on the gas phase distribution.When the inclination angle is 50°,the relative power demand reaches the maximum.An appropriate increase in the impeller distance from the bottom improves the gas holdup and gas phase distribution but increases the liquid phase mixing time.
