Heat Transfer and Pressure Drop Studies of Vertical Gas-Particle Flow Using a Variable Gas Property Two-Fluid Model

被引:1
作者
Patro, Brundaban [1 ]
Kupireddi, Kiran Kumar [1 ]
Devanuri, Jaya Krishna [1 ]
机构
[1] Natl Inst Technol Warangal, Dept Mech Engn, Hanumakonda 506004, Telangana, India
关键词
Particulate flows; Nusselt number; Pressure drop; Two-fluid model; Vertical pipe; PIPE; PREDICTION; SUSPENSION; MASS;
D O I
10.1007/s40997-022-00561-6
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
In the current work, the two-fluid model with variable gas properties is used to predict heat transfer and pressure drop in a vertical, adiabatic pipe. The simulation outcomes are compared between the variable and constant gas properties models. The simulation outcomes confirm that there is an insignificant deviation in the results of heat transfer, but there is a considerable deviation in the pressure drop data between the variable and constant gas properties models. The results also show that the restitution coefficients and specularity coefficient do not affect the simulation results. The effects of particle size, loading ratio, and inlet gas velocity on the thermo-hydrodynamic characteristics of gas-particle flows are studied. The simulation results show that there is enhanced heat transfer with increasing the gas-phase Reynolds number. Moreover, the gas-phase Prandtl number variation is not affected by the flow parameters. Finally, a correlation is proposed to predict the two-phase Nusselt number.
引用
收藏
页码:893 / 903
页数:11
相关论文
共 31 条
[1]  
ANSYS FLUENT Inc, 2015, FLUENT US GUID
[2]   NUMERICAL MODELING OF HEAT TRANSFER FOR GAS-SOLID FLOW IN VERTICAL PIPES [J].
Azizi, Salar ;
Taheri, Mansour ;
Mowla, Dariush .
NUMERICAL HEAT TRANSFER PART A-APPLICATIONS, 2012, 62 (08) :659-677
[3]   Prediction of heat transfer in a turbulent gas-solid pipe flow using a two-fluid model [J].
Boulet, P ;
Oesterlé, B ;
Tanière, A .
PARTICULATE SCIENCE AND TECHNOLOGY, 1999, 17 (04) :253-267
[4]  
Dixon J.C., 2007, The Shock Absorber Handbook, DOI DOI 10.1002/9780470516430
[5]   Prediction of Pressure Drop in Vertical Pneumatic Conveyors [J].
El-Behery, S. M. ;
El-Haroun, A. A. ;
Abuhegazy, M. R. .
JOURNAL OF APPLIED FLUID MECHANICS, 2017, 10 (02) :519-527
[6]   Numerical and experimental studies of heat transfer in particle-laden gas flows through a vertical riser [J].
El-Behery, Samy M. ;
El-Askary, W. A. ;
Hamed, Mofreh H. ;
Ibrahim, K. A. .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2012, 33 (01) :118-130
[7]   Hydrodynamic and thermal fields analysis in gas-solid two-phase flow [J].
El-Behery, Samy M. ;
El-Askary, W. A. ;
Hamed, Mofreh H. ;
Ibrahim, K. A. .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2011, 32 (03) :740-754
[8]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[9]   Heat transfer from a single tube to the flowing gas-solid suspension in a CFB riser [J].
Everaert, K. ;
Baeyens, J. ;
Smolders, K. .
HEAT TRANSFER ENGINEERING, 2006, 27 (06) :66-70
[10]  
Gidaspow D., 1994, MULTIPHASE FLOW FLUI