A comparison of fuzzy logic and cluster renewal approaches for heat transfer modeling in a 1296 t/h CFB boiler with low level of flue gas recirculation

被引:44
作者
Błaszczuk A. [1 ]
Krzywański J. [2 ]
机构
[1] Institute of Advanced Energy Technologies, Czestochowa University of Technology, Dabrowskiego 73, Czestochowa
[2] Jan Dlugosz University in Czestochowa, Faculty of Mathematics and Natural Sciences, Armii Krajowej 13/15, Czestochowa
关键词
Circulating fluidized bed; Cluster renewal approach; Flue gas recirculation; Fuzzy logic; Heat transfer coefficient;
D O I
10.1515/aoter-2017-0006
中图分类号
学科分类号
摘要
The interrelation between fuzzy logic and cluster renewal approaches for heat transfer modeling in a circulating fluidized bed (CFB) has been established based on a local furnace data. The furnace data have been measured in a 1296 t/h CFB boiler with low level of flue gas recirculation. In the present study, the bed temperature and suspension density were treated as experimental variables along the furnace height. The measured bed temperature and suspension density were varied in the range of 1131-1156 K and 1.93-6.32 kg/m3, respectively. Using the heat transfer coefficient for commercial CFB combustor, two empirical heat transfer correlation were developed in terms of important operating parameters including bed temperature and also suspension density. The fuzzy logic results were found to be in good agreement with the corresponding experimental heat transfer data obtained based on cluster renewal approach. The predicted bed-to-wall heat transfer coefficient covered a range of 109-241 W/(m2K) and 111-240 W/(m2K), for fuzzy logic and cluster renewal approach respectively. The divergence in calculated heat flux recovery along the furnace height between fuzzy logic and cluster renewal approach did not exceeded ±2%.
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页码:91 / 122
页数:31
相关论文
共 68 条
[31]  
Mahalingam M., Kolar A.K., Emulsion layer model for wall heat transfer in a circulating fluidized bed, AIChE, 37, 8, pp. 1139-1150, (1991)
[32]  
Hua Y., Flamant G., Lu J., Gauthier D., Modeling of axial and radial solid segregation in a CFB boiler, Chem. Eng. Process., 43, 8, pp. 971-978, (2004)
[33]  
Blaszczuk A., Zylka A., Leszczynski J., Simulation of mass balance behavior in a large-scale circulating fluidized bed reactor, Particuology, 25, pp. 51-58, (2016)
[34]  
Basu P., Fraser S., Circulating Fluidized Bed Boiler-Design and Operation, (1991)
[35]  
Johansson A., Johnsson F., Leckner B., Solids back-mixing in CFB boilers, Chem. Eng. Sci., 62, 1-2, pp. 561-573, (2007)
[36]  
Zhang W., Johnsson F., Leckner B., Fluid-dynamic boundary layers in CFB boilers, Chem. Eng. Sci., 50, 2, pp. 201-210, (1995)
[37]  
Harris A.T., Davidson J.F., A core-annulus deposition model for circulating fluidized bed risers, Circulating Fluidized Bed Technology IV, (1994)
[38]  
Horio M., Hydrodynamics, Circulating Fluidized Bed, (1997)
[39]  
Blaszczuk A., Nowak W., Bed-to-wall heat transfer coefficient in a supercritical CFB boiler at different bed particle sizes, Int. J. Heat Mass Tran., 79, pp. 736-749, (2014)
[40]  
Vijay G.N., Reddy B.V., Effect of dilute and dense phase operating conditions on bed-to-wall heat transfer mechanism in a circulating fluidized bed combustor, Int. J. Heat Mass Tran., 48, 16, pp. 3276-3283, (2005)