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Modeling Study on Non-Uniform Lateral Distribution in Large-Scale Circulating Fluidized Bed Boilers
被引:0
作者:
Deng, Boyu
[1
]
Zhang, Yi
[2
]
Zhang, Man
[1
]
Yang, Hairui
[1
]
Yue, Guangxi
[1
]
机构:
[1] Tsinghua Univ, Dept Energy & Power Engn, State Key Lab Power Syst, Beijing 100084, Peoples R China
[2] China Elect Power Planning & Amp Engn Inst, Beijing 100120, Peoples R China
关键词:
2D modeling;
Fluidization model;
Large-scale CFB boilers;
Lateral dispersion;
Non-uniform distribution;
CHEMICAL LOOPING COMBUSTION;
FIBER REFLECTION PROBES;
UPPER DILUTE ZONE;
SEWAGE-SLUDGE;
VOLUME CONCENTRATION;
FLOWSHEET SIMULATION;
2-DIMENSIONAL MODEL;
CATALYST ATTRITION;
CAPACITANCE PROBE;
OXYGEN CARRIER;
D O I:
10.1002/cite.202200078
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
With the development of the circulating fluidized bed (CFB) combustion technology, the cross-sectional area of the boiler furnace increases gradually, making the lateral non-uniform distribution in the furnace more prominent. To investigate the flow field inhomogeneity in the furnace, a two-dimensional mass balance model was established in this work, and the lateral solid concentration deviation was adopted to evaluate the degree of the flow field inhomogeneity. Afterwards, the effect of four factors on the lateral non-uniform distribution was examined. It turned out that the lateral profile of the primary air flow rate had a much greater influence than that of the coal feeding rate.
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页码:114 / 121
页数:8
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