Realization and Control of Multiple Temperature Zones in Liquid-Containing Gas-Solid Fluidized Bed Reactor

被引:34
作者
Zhou, Yefeng [1 ,2 ,3 ]
Shi, Qiang [1 ,2 ]
Huang, Zhengliang [1 ,2 ]
Liao, Zuwei [1 ,2 ]
Wang, Jingdai [1 ,2 ]
Yang, Yongrong [1 ,2 ]
机构
[1] Zhejiang Univ, State Key Lab Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
[2] Zhejiang Univ, Dept Chem Engn, Coll Chem & Biol Engn, Hangzhou 310027, Zhejiang, Peoples R China
[3] Xiangtan Univ, Dept Chem Engn, Xiangtan 411105, Hunan, Peoples R China
基金
中国国家自然科学基金;
关键词
multiple temperature zones; liquid-containing gas-solid fluidized bed reactor; realization and control; liquid evaporation and liquid bridge; multiple measurement techniques; CHEMICAL-LOOPING COMBUSTION; PRESSURE-FLUCTUATIONS; BEHAVIOR; BUBBLE;
D O I
10.1002/aic.15157
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluidized bed reactors (FBRs) have been developed to establish multiple temperature zones for various industrial processes. To overcome the common weakness, this work proposed to spray liquid into bottom and upper zones, respectively, to realize multiple temperature zones FBR (MTZFBR). Temperature, pressure, and acoustic emission techniques were applied to fully characterize liquid interaction and hydrodynamics. Compared with the bottom liquid-spraying approach, the upper liquid-spraying approach showed higher temperature difference (DT) and better fluidization stability, thus was selected for further control studies. Effects of liquid flow rate, static bed height, and inlet gas temperature on MTZFBR were studied systematically. The results showed that increasing liquid evaporation behavior or decreasing liquid bridge behavior enhance DT and fluidization stability and vice versa. G-L-S fluidization pattern depended mostly on the liquid behaviors and fluidization stability, and thus the stabilized MTZFBR could be regarded as a coexisted mode of two distinctive G-L-S fluidization patterns. (C) 2016 American Institute of Chemical Engineers
引用
收藏
页码:1454 / 1466
页数:13
相关论文
共 31 条
[1]   Progress in Chemical-Looping Combustion and Reforming technologies [J].
Adanez, Juan ;
Abad, Alberto ;
Garcia-Labiano, Francisco ;
Gayan, Pilar ;
de Diego, Luis F. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2012, 38 (02) :215-282
[2]   Fluidized bed granulation - the importance of a drying zone for the particle growth mechanism [J].
Becher, RD ;
Schlunder, EU .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1998, 37 (01) :1-6
[3]   The uses of passive measurement of acoustic emissions from chemical engineering processes [J].
Boyd, JWR ;
Varley, J .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (05) :1749-1767
[4]  
Chen J, 2005, CATALYTIC CRAKING TE
[5]   Particle granular temperature in gas fluidized beds [J].
Cody, GD ;
Goldfarb, DJ ;
Storch, GV ;
Norris, AN .
POWDER TECHNOLOGY, 1996, 87 (03) :211-232
[6]   The multizone circulating reactor technology [J].
Covezzi, M ;
Mei, G .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (13) :4059-4067
[7]   Frontiers in Reactor Engineering [J].
Dudukovic, Milorad P. .
SCIENCE, 2009, 325 (5941) :698-701
[8]  
Fan L.S., 1989, GAS LIQUID SOLID FLU
[9]   Fluidized bed reactors with two-zones for maleic anhydride production:: Different configurations and effect of scale [J].
Gascón, J ;
Téllez, C ;
Herguido, J ;
Menéndez, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (24) :8945-8951
[10]  
Govoni, 2004, [No title captured], Patent No. [US 6,689,845 B1, 6689845]