Two-fluid modeling of turbulent particle-gas suspensions in vertical pipes

被引:23
|
作者
Patro, Pandaba [1 ]
Dash, Sukanta K. [1 ]
机构
[1] IIT Kharagpur, Dept Mech Engn, Kharagpur 721302, W Bengal, India
关键词
Gas-solid flow; Pressure drop; Two-fluid modeling; Kinetic theory; Particulate loading; NUMERICAL-SIMULATION; PRESSURE-DROP; FLOW; PREDICTIONS;
D O I
10.1016/j.powtec.2014.05.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Numerical simulations of dilute, turbulent gas-solid flows in vertical pipes are performed using a two-fluid model or Euler-Euler model incorporating kinetic theory for granular flows (KTGF) and accounting for a four-way coupling (i.e. consideration of particle-particle collisions along with gas-particle interactions). Comparison of the model predictions with experimental data reveals good agreement. The paper mainly focuses on the investigation of fully developed velocity profiles; turbulent intensity and pressure drop over a wide range of operating conditions and particle properties. The significant contribution of the present study is the development of a correlation for pressure drop in vertical gas-solid flows using non-linear regression analysis from the data obtained from CFD predictions, which gives an accuracy of +/- 15%. This correlation can be used for the prediction of pressure drop in pneumatic conveying of fly ash, cement, pulverized coal etc. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:320 / 331
页数:12
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