Flow rate of solids through recycle chamber of loop seal in a circulating fluidized bed

被引:2
作者
Lee, Dong Hun [1 ]
Kim, Daewook [2 ]
Won, Yoo Sube [2 ]
Choi, Jeong-Hoo [1 ]
Joo, Ji Bong [1 ]
Ryu, Ho-Jung [2 ]
机构
[1] Konkuk Univ, Dept Chem Engn, 120 Neungdong Ro, Seoul 05029, South Korea
[2] Korea Inst Energy Res, 152 Gajeong Ro, Daejeon 34129, South Korea
关键词
Solids flow rate; Solids circulation rate; Recycle chamber; Loop seal; Circulating fluidized bed; PRESSURE-DROP; PARTICLE PROPERTIES; HYDRODYNAMIC MODEL; GAS; IMPACT; PERFORMANCE; RISER; SIDE;
D O I
10.1016/j.apt.2023.104140
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study investigated the flow rate of solids through the recycle chamber of a loop seal in a circulating fluidized bed (CFB) at atmospheric pressure and temperature. Flow characteristics of alumina particles were measured in the downcomer, horizontal passage, recycle chamber, and riser (0.05 m i.d., 2.7 m high).As the gas velocity in the riser increased, the pressure drop in the downcomer decreased, and thus, the aeration rate required at the bottom of the supply chamber to attain the minimum fluidization state for the bed of the downcomer increased. Based on experimental data, relationships that could predict the flow rate of solids through the recycle chamber Gs,r were derived by extending the correlation for the solids flow rate through the bubbling fluidized bed that discharged solids via overflow exit. Gs,r increased in proportion to the gauge pressure at the base of the recycle chamber. When the riser was under the fast bed condition, the back pressure against the flow of solids coming from the recycle chamber to the riser appeared significantly, and Gs,r was inversely proportional to the gauge pressure at the base of the riser. The derived relationships for Gs,r were in good agreement with measured data.& COPY; 2023 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved. All rights reserved.
引用
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页数:9
相关论文
共 37 条
[1]  
Arjunwadkar A., 2015, PROC 22 INT C FLUIDI, P246
[2]   SATURATION CARRYING-CAPACITY OF GAS AND FLOW REGIMES IN CFB [J].
BAI, DL ;
KATO, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1995, 28 (02) :179-185
[3]   Gas and solid flow patterns in the loop-seal of a circulating fluidized bed [J].
Bareschino, Piero ;
Solimene, Roberto ;
Chirone, Riccardo ;
Salatino, Piero .
POWDER TECHNOLOGY, 2014, 264 :197-202
[4]   An analysis of loop seal operations in a circulating fluidized bed [J].
Basu, P ;
Cheng, L .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2000, 78 (A7) :991-998
[5]   Studies on the operation of loop-seal in circulating fluidized bed boilers [J].
Basu, Prabir ;
Butler, James .
APPLIED ENERGY, 2009, 86 (09) :1723-1731
[6]   TYPES OF CHOKING IN VERTICAL PNEUMATIC SYSTEMS [J].
BI, HT ;
GRACE, JR ;
ZHU, JX .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1993, 19 (06) :1077-1092
[7]   Effect of pressure on loop seal operation for a pressurized circulating fluidized bed [J].
Cheng, LM ;
Basu, P .
POWDER TECHNOLOGY, 1999, 103 (03) :203-211
[8]   An investigation of performance of a conventional U type loop-seal for CFB reactors with side and bottom aerations [J].
Chinsuwan, Anusorn ;
Somjun, Jiraroch .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2020, 163 :58-66
[9]   Generalized model for bubble size and frequency in gas-fluidized beds [J].
Choi, JH ;
Son, JE ;
Kim, SD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (06) :2559-2564
[10]   Elimination of stagnant particles from a N-valve with side aeration in circulating fluidized bed [J].
Dong, Li ;
Ji, Wenfeng ;
Zhao, Zhigang ;
Xu, Guangwen .
ADVANCED POWDER TECHNOLOGY, 2014, 25 (03) :1155-1161