Numerical simulation of heat transfer coefficient around different immersed bodies in a fluidized bed containing Geldart B particles

被引:22
作者
Fattahi, Mohsen [1 ]
Hosseini, Seyyed Hossein [2 ]
Ahmadi, Goodarz [3 ]
Parvareh, Arsalan [4 ]
机构
[1] Univ Kurdistan, Dept Chem Engn, Sanandaj, Iran
[2] Ilam Univ, Dept Chem Engn, Ilam 69315516, Iran
[3] Clarkson Univ, Dept Mech & Aeronaut Engn, Potsdam, NY 13699 USA
[4] Razi Univ, Dept Chem Engn, Fac Petr & Chem Engn, Kermanshah 6714967346, Iran
关键词
Gas-solid fluidized beds; Surface-to-bed HTC; CFD; TFM; Immersed bodies; HORIZONTAL TUBE; FRACTION PROFILES; KINETIC-THEORY; WALL; SURFACE; HYDRODYNAMICS; FLOW; PREDICTION; BEHAVIOR; MODEL;
D O I
10.1016/j.ijheatmasstransfer.2019.06.058
中图分类号
O414.1 [热力学];
学科分类号
摘要
Using the Eulerian-Eulerian two-fluid model (TFM) the hydrodynamics and heat transfer around different immersed bodies in a fluidized bed were analyzed. The kinetic theory of granular flow (KTGF) was used to simulate the solid phase. For hydrodynamic simulations, 3D, 2D Cartesian and 2D axisymmetric frameworks were examined and the differences in the results of these simulations were discussed. For the heat transfer analysis, due to the high computational demand of 3D simulations, the analyses were performed using 2D Cartesian and axisymmetric frameworks. For studying the effect of shape on the CFD results, two cases of spherical and cylindrical immersed bodies were simulated. In addition, two methods for calculating the surface-to-bed heat transfer coefficient (HTC) for 2D Cartesian and axisymmetric models were examined. The first (method I) is based on constant heat flux boundary condition, while the second one (method II) is based on the isothermal wall boundary condition. It was found that method I outperforms the second one for both 2D Cartesian and axisymmetric configurations in prediction of average HTC. It was shown that the simulation results were in closed agreement with the corresponding measured data. The findings revealed that the spherical immersed body, which has a better aerodynamic shape, produced higher HTC in bubbling fluidized bed with Geldart B particles. Finally, the impact of Archimedes number (Ar) on the surface-to-bed HTC was studied. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:353 / 366
页数:14
相关论文
共 68 条
[1]   Influence of the specularity coefficient on hydrodynamics and heat transfer in a conical fluidized bed combustor [J].
Abdelmotalib, Hamada M. ;
Youssef, Mahmoud A. M. ;
Hassan, Ali Ahmed ;
Youn, Suk Bum ;
Im, Ik-Tae .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2016, 75 :169-176
[2]   A study on wall-to-bed heat transfer in a conical fluidized bed combustor [J].
Abdelmotalib, Hamada Mohamed ;
Ko, Dong Guk ;
Im, Ik-Tae .
APPLIED THERMAL ENGINEERING, 2016, 99 :928-937
[3]   Three dimensional modeling of heat transfer and bed flow in a conical fluidized bed reactor [J].
Abdelmotalib, Hamada Mohmmed ;
Im, Ik-Tae .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2017, 106 :1335-1344
[4]   Local heat transfer coefficients around a horizontal heated tube immersed in a gas fluidized bed [J].
Al-Busoul, MA ;
Abu-Ein, SK .
HEAT AND MASS TRANSFER, 2003, 39 (04) :355-358
[6]   The influence of multiple tubes on the tube-to-bed heat transfer in a fluidised bed [J].
Armstrong, L. M. ;
Gu, S. ;
Luo, K. H. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2010, 36 (11-12) :916-929
[7]   Study of wall-to-bed heat transfer in a bubbling fluidised bed using the kinetic theory of granular flow [J].
Armstrong, L. M. ;
Gu, S. ;
Luo, K. H. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2010, 53 (21-22) :4949-4959
[8]   Local heat-transfer coefficient of immersed cylindrical surface in fluidized and vibrated fluidized beds [J].
Bacelos, M. S. ;
Camargo, C. F. S. ;
Silveira, A. M. ;
Freire, J. T. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2011, 50 (11-12) :1152-1159
[9]   Eulerian-Eulerian simulation of dense solid-gas cylindrical fluidized beds: Impact of wall boundary condition and drag model on fluidization [J].
Bakshi, A. ;
Altantzis, C. ;
Bates, R. B. ;
Ghoniem, A. F. .
POWDER TECHNOLOGY, 2015, 277 :47-62
[10]   Heat transfer in fluidized beds with immersed surface: Effect of geometric parameters of surface [J].
Bisognin, Priscilla Correa ;
Fusco, Jose Mozart ;
Soares, Cintia .
POWDER TECHNOLOGY, 2016, 297 :401-408