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.
引用
收藏
页码:114 / 121
页数:8
相关论文
共 71 条
[51]   MASS-TRANSFER AND REACTION BEHAVIOR OF A CIRCULATING FLUIDIZED-BED REACTOR [J].
VOLLERT, J ;
WERTHER, J .
CHEMICAL ENGINEERING & TECHNOLOGY, 1994, 17 (03) :201-209
[52]   Syngas, tar and char behavior in chemical looping gasification of sawdust pellet in fluidized bed [J].
Wang, Shen ;
Song, Tao ;
Yin, Shangyi ;
Hartge, Ernst-Ulrich ;
Dymala, Timo ;
Shen, Laihong ;
Heinrich, Stefan ;
Werther, Joachim .
FUEL, 2020, 270
[53]   RADIAL GAS MIXING IN THE UPPER DILUTE CORE OF A CIRCULATING FLUIDIZED-BED [J].
WERTHER, J ;
HARTGE, EU ;
KRUSE, M .
POWDER TECHNOLOGY, 1992, 70 (03) :293-301
[54]   Sewage sludge combustion [J].
Werther, J ;
Ogada, T .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 1999, 25 (01) :55-116
[55]   Measurement techniques in fluidized beds [J].
Werther, J .
POWDER TECHNOLOGY, 1999, 102 (01) :15-36
[56]   CONVECTIVE SOLIDS TRANSPORT IN LARGE DIAMETER GAS-FLUIDIZED BEDS [J].
WERTHER, J .
POWDER TECHNOLOGY, 1976, 15 (02) :155-167
[57]   Modeling of industrial fluidized-bed reactors [J].
Werther, J ;
Hartge, EU .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (18) :5593-5604
[58]   JET ATTRITION OF CATALYST PARTICLES IN GAS-FLUIDIZED BEDS [J].
WERTHER, J ;
XI, W .
POWDER TECHNOLOGY, 1993, 76 (01) :39-46
[59]   MODELING AND SCALE-UP OF INDUSTRIAL FLUIDIZED-BED REACTORS [J].
WERTHER, J .
CHEMICAL ENGINEERING SCIENCE, 1980, 35 (1-2) :372-379
[60]   Emissions from sewage sludge combustion in Germany - Status and future trends [J].
Werther, J ;
Saenger, M .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2000, 33 (01) :1-11