Experimental study and X-ray microtomography based CFD simulation for the characterization of pressure drop in sinter bed

被引:16
作者
Zhou, Hao [1 ]
Zhou, Mingxi [1 ]
Cheng, Ming [1 ]
Guo, Wushuang [1 ]
Cen, Kefa [1 ]
机构
[1] Zhejiang Univ, Inst Thermal Power Engn, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
基金
中国国家自然科学基金;
关键词
X-ray microtomography; CFD simulation; Porous structure; Pressure drop; Iron ore sintering; LATTICE-BOLTZMANN SIMULATION; IRON-ORE; FLUID-FLOW; COMBUSTION CHARACTERISTICS; PORE STRUCTURE; PARTICLE-SIZE; HEAT-TRANSFER; METAL FOAMS; PACKED-BEDS; AIR-FLOW;
D O I
10.1016/j.applthermaleng.2016.10.123
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this study, pilot-scale sinter pot tests under three granulation moisture conditions were conducted. Porous structures of the sampled sinter cakes were reconstructed by X-ray microtomography and CFD simulations were applied based on the real geometry. The pressure drop of serial subzones along the sinter bed including sintered zone, high-temperature zone and humidified zone were discussed by analyzing the experimental measured airflow rate and CFD simulation results together. The results show that sinter cake porosity increases from 0.48 at 6.3 wt% H2O to 0.59 at 7.3 wt% H2O. The reconstructed sinter cakes show various complex porous structures, resulting in remarkable flow heterogeneity and complicated velocity field. A high porosity bed has many more gas channels and the flow distribution is developed better. The pressure drop in sintered zone is similar to 1.5 kPa/m, which is much lower compared to the high temperature zone and humidified zone. The high-temperature zone where main reactions and bed structure changes happen has a controlling effect on the pressure drop across the sinter bed. The sintering bed permeability greatly determines the final productivity, which is affected by the bed temperature profile and bed porous structure. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:811 / 819
页数:9
相关论文
共 33 条
[1]   Syngas production from downdraft gasification of oil palm fronds [J].
Atnaw, Samson Mekbib ;
Sulaiman, Shaharin Anwar ;
Yusup, Suzana .
ENERGY, 2013, 61 :491-501
[2]   Three Dimensional Mathematical Model of the Iron Ore Sintering Process Based on Multiphase Theory [J].
de Castroa, Jose Adilson ;
Sazaki, Yasushi ;
Yagi, Jun-ichiro .
MATERIALS RESEARCH-IBERO-AMERICAN JOURNAL OF MATERIALS, 2012, 15 (06) :848-858
[3]   Investigation of factors affecting channelling in fixed-bed solid fuel combustion using CFD [J].
Duffy, Neil T. M. ;
Eaton, John A. .
COMBUSTION AND FLAME, 2013, 160 (10) :2204-2220
[4]   Effect of ore properties on sinter bed permeability and strength [J].
Ellis, B. G. ;
Loo, C. E. ;
Witchard, D. .
IRONMAKING & STEELMAKING, 2007, 34 (02) :99-108
[5]   CFD modelling of bed shrinkage and channelling in fixed-bed combustion [J].
Hermansson, Sven ;
Thunman, Henrik .
COMBUSTION AND FLAME, 2011, 158 (05) :988-999
[6]   Characterisation of tars from biomass gasification: Effect of the operating conditions [J].
Hernandez, J. J. ;
Ballesteros, R. ;
Aranda, G. .
ENERGY, 2013, 50 :333-342
[7]   X-ray computed tomography reconstruction and analysis of polymer electrolyte membrane fuel cell porous transport layers [J].
James, J. P. ;
Choi, H. -W. ;
Pharoah, J. G. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (23) :18216-18230
[8]   NEW ANALYSIS METHOD OF SINTER CAKE PORE STRUCTURE FOR PERMEABILITY EVALUATION [J].
KASAMA, S ;
INAZUMI, T ;
NAKAYASU, T .
ISIJ INTERNATIONAL, 1994, 34 (07) :562-569
[9]   Quantifying the resistance to airflow during iron ore sintering [J].
Loo, CE ;
Hutchens, MF .
ISIJ INTERNATIONAL, 2003, 43 (05) :630-636
[10]  
Loo CE, 2002, T I MIN METALL C, V111, pC11