Coupled modeling of combustion and hydrodynamics for a coal-fired supercritical boiler

被引:44
作者
Chen, Tang [1 ]
Zhang, Yan-jun [1 ]
Liao, Meng-ran [1 ]
Wang, Wei-zong [1 ]
机构
[1] Beihang Univ, Sch Astronaut, Beijing 100191, Peoples R China
关键词
CFD; Coupled simulation; Pendant superheater; Ultra-supercritical boiler; CHEMICAL PERCOLATION MODEL; FLUID-FLOW; SIMULATION; FURNACE; STEAM; DEVOLATILIZATION;
D O I
10.1016/j.fuel.2018.11.008
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Computational fluid dynamics (CFD) model of coal combustion is coupled with the one-dimensional hydrodynamic model of supercritical steam, and applied in the simulation of the superheater. The convective heat exchangers are neglected. Complex tube arrangements can be modeled with the aid of AutoCAD, and therefore the simulation could offer detailed information on heat exchangers. It is found that the outlet steam temperature of the tube is very sensitive to the variation of ash deposit temperature. Therefore it is not reasonable to use decoupled method for predicting the energy flux transported to the steam. The outlet steam temperature of a row of tubes is compared with the running data from the power plant. The simulation result fits well with running data. Nevertheless, one can impose an average steam temperature plus 50 K as the tube outside surface temperature; then calculates the temperature of the ash deposit according to the thermal resistance of ash deposit and energy flux. The result from this "simplified" coupled method is very close to fully coupled method.
引用
收藏
页码:49 / 56
页数:8
相关论文
共 33 条
[1]   Numerical simulation of brown coal combustion in a 550 MW tangentially-fired furnace under different operating conditions [J].
Al-Abbas, Audai Hussein ;
Naser, Jamal ;
Hussein, Emad Kamil .
FUEL, 2013, 107 :688-698
[2]   CFD modelling of air-fired and oxy-fuel combustion in a large-scale furnace at Loy Yang A brown coal power station [J].
Al-Abbas, Audai Hussein ;
Naser, Jamal ;
Dodds, David .
FUEL, 2012, 102 :646-665
[3]  
[Anonymous], 2007, DESIGN AND OPERATION
[4]   A THEORY OF FLUID FLOW IN COMPLAINT TUBES [J].
BARNARD, ACL ;
HUNT, WA ;
TIMLAKE, WP ;
VARLEY, E .
BIOPHYSICAL JOURNAL, 1966, 6 (06) :717-&
[5]   PREDICTING COMBUSTION BEHAVIOUR OF COAL PARTICLES [J].
BAUM, MM ;
STREET, PJ .
COMBUSTION SCIENCE AND TECHNOLOGY, 1971, 3 (05) :231-&
[6]   TURBULENT DISPERSION OF PARTICLES - THE STP MODEL [J].
BAXTER, LL ;
SMITH, PJ .
ENERGY & FUELS, 1993, 7 (06) :852-859
[7]  
CHURCHILL SW, 1977, CHEM ENG-NEW YORK, V84, P91
[8]   Numerical study of a 350 MWe tangentially fired pulverized coal furnace of the As Pontes Power Plant [J].
Constenla, I. ;
Ferrin, J. L. ;
Saavedra, L. .
FUEL PROCESSING TECHNOLOGY, 2013, 116 :189-200
[9]   Numerical investigation of firing concepts for a flexible Greek lignite-fired power plant [J].
Drosatos, Panagiotis ;
Nikolopoulos, Nikolaos ;
Agraniotis, Michalis ;
Kakaras, Emmanouil .
FUEL PROCESSING TECHNOLOGY, 2016, 142 :370-395
[10]   An integrated computational fluid dynamics-process model of natural circulation steam generation in a coal-fired power plant [J].
Edge, P. J. ;
Heggs, P. J. ;
Pourkashanian, M. ;
Williams, A. .
COMPUTERS & CHEMICAL ENGINEERING, 2011, 35 (12) :2618-2631