Calculation of terminal velocity in transitional flow for spherical particle

被引:0
作者
Zhang Lei [1 ,2 ]
Honaker Ricky [2 ]
Liu Wenli [1 ]
Men Dongpo [1 ]
Chen Jinxiang [2 ]
机构
[1] School of Chemical and Environmental Engineering,China University of Mining & Technology
[2] Department of Mining Engineering,University of Kentucky
关键词
Transitional flow; Drag coefficient; Terminal velocity; Spherical particle; Calculation;
D O I
暂无
中图分类号
O35 [流体力学];
学科分类号
080103 ; 080704 ;
摘要
The terminal velocity has been widely used in extensive fields,but the complexity of drag coefficient expression leads to the calculation of terminal velocity in transitional flow e1 < Re 6 1000 T with much more difficulty than those in laminar flow eRe 6 1T and turbulent flow eRe P 1000 T.This paper summarized and compared 24 drag coefficient correlations,and developed an expression for calculating the terminal velocity in transitional flow,and also analyzed the effects of particle density and size,fluid density and viscosity on terminal velocity.The results show that 19 of 24 previously published correlations for drag coefficient have good prediction performance and can be used for calculating the terminal velocity in the entire transitional flow with higher accuracy.Adapting two dimensionless parameters(w*,d*),a proposed explicit correlation,w*=-25:68654 exp(-d*/77:02069)+24:89826,is attained in transitional flow with good performance,which is helpful in calculating the terminal velocity.
引用
收藏
页码:311 / 317
页数:7
相关论文
共 12 条
[1]  
Numerical simulation and experimental verification of bubble size distribution in an air dense medium fluidized bed[J]. He Jingfeng,Zhao Yuemin,Luo Zhenfu,He Yaqun,Duan Chenlong. International Journal of Mining Science and Technology. 2013(03)
[2]  
Experiment and simulation on the pyrite removal from the recirculating load of pulverizer with a dilute phase gas-solid fluidized bed[J]. Wang Shuai,He Yaqun,He Jingfeng,Ge Linhan,Liu Qing. International Journal of Mining Science and Technology. 2013(02)
[3]  
Effect of the column height on the performance of liquid-solid fluidized bed for the separation of coarse slime[J]. Sha Jie a,,Xie Guangyuan a,Wang Hong b,Liu Junzhang b,Tang Ligang c a School of Chemical Engineering and Technology,China University of Mining & Technology,Xuzhou 221008,China b Beijing Huayu Engineering Co.Ltd.,Pingdingshan 467000,China c State Key Laboratory of Multiphase Complex Systems,Institute of Process Engineering,Chinese Academy of Sciences,Beijing 100190,China. Internati
[4]  
Numerical simulation of the pulsing air separation field based on CFD[J]. He Jingfeng,He Yaqun,Zhao Yuemin,Duan Chenlong,Ye Cuiling School of Chemical Engineering and Technology,China University of Mining & Technology,Xuzhou 221116,China. International Journal of Mining Science and Technology. 2012(02)
[5]  
The drag coefficient of a sphere: An approximation using shanks transform[J] . M.D. Mikhailov,A.P. Silva Freire. Powder Technology . 2012
[6]  
Comparison of formulas for drag coefficient and settling velocity of spherical particles[J] . Nian-Sheng Cheng. Powder Technology . 2008 (3)
[7]  
Drag coefficient of flow around a sphere: Matching asymptotically the wide trend[J] . Jaber Almedeij. Powder Technology . 2008 (3)
[8]  
Drag coefficient and settling velocity for particles of cylindrical shape[J] . Jorge Gabitto,Costas Tsouris. Powder Technology . 2007 (2)
[9]  
A new model for estimation of drag force in the flow of Newtonian fluids around rigid or deformable particles[J] . Powder Technology . 2001 (2)
[10]  
THE RESISTANCE TO MOTION OF A SOLID SPHERE IN A FLUID[J] . A.R. Khan,J.F. Richardson. Chemical Engineering Communications . 1987 (1-6)