摘要
利用商业CFD软件Fluent12.0和并行计算系统图形工作站,对改进的Intermig桨种分槽内部流场进行了三维数值解析.采用Realizablekε湍流模型和欧拉欧拉多相流模型对槽内不同桨叶离底距离C、桨叶直径D下的氢氧化铝颗粒悬浮规律以及搅拌桨功率消耗进行了模拟.结果显示,搅拌转速一定的条件下,桨叶直径越大,越有利于颗粒悬浮,搅拌功率越大;相对最佳桨径与槽径比为0.6;过高和过低的桨叶离底距离都不利于氢氧化铝颗粒悬浮,桨叶离底距离对功率影响较小,相对最佳离底距离与桨径比为0.55.
Seed precipitation tank with a new-style improved Intermig impeller was numerically simulated by using the commercial software Fluent 12.0 on parallel computing graphic workstation.The suspension of Al(OH)3 particles and power consumption in the alumina seed precipitator under different conditions of the impeller off-bottom clearance height (C) and blade diameter (D) were numerically simulated by using realizable k-ε turbulence,Eulerian Eulerian multiphase and multi-reference frame rotating models.The numerical simulation results showed that at a constant rotate speed,enlarging D was good for suspension of Al(OH)3 particles,but bigger D resulted in more power consumption.The optimal value of D/T was 0.6,T was the tank diameter.Too big or too small C was not conducive to the suspension of Al(OH)3 particles,and C had little effect on the stirring power.The optimal value of C/D was 0.55.
出处
《过程工程学报》
CAS
CSCD
北大核心
2011年第1期15-19,共5页
The Chinese Journal of Process Engineering
基金
国家自然科学基金资助项目(编号:50974035)
国家重点基础研究发展规划资助项目(编号:2007CB613504)
中国博士后科学基金资助项目(编号:20090451277)
教育部高校博士点专项基金资助项目(编号:20050145029)
辽宁省青年人才基金资助项目(编号:2005221012)
辽宁省财政厅/省计划资助项目(编号:200921007)
关键词
种分槽
机械搅拌
数值模拟
氢氧化铝颗
固液两相流
seed precipitation tank
mechanical stirring
numerical simulation
Al(OH)3 particles
solid liquid phase flow