Effect of particle size distribution on agglomeration/defluidization during fluidized bed combustion

被引:52
作者
Lin, Chiou-Liang [1 ]
Peng, Tzu-Huan [1 ]
Wang, Wei-Jen [1 ]
机构
[1] Natl Univ Kaohsiung, Dept Civil & Environm Engn, Kaohsiung 811, Taiwan
关键词
Agglomeration; Defluidization; Combustion; Fluidized bed; Particle size; TEMPERATURE GAS FLUIDIZATION; OPERATING-CONDITIONS; IRON PARTICLES; AGGLOMERATION; DEFLUIDIZATION; WASTE; INCINERATION; ASH; GASIFICATION; MINIMUM;
D O I
10.1016/j.powtec.2010.11.010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study focused on the effect of particle size distribution (PSD) on agglomeration and defluidization in a fluidized bed. The four PSDs studied were narrow, Gaussian, binary and flat. The experimental variables studied included the gas velocity, the operating temperature, the Na concentration and the addition of Ca. The defluidization time decreased with increasing operating temperature and Na concentration, and these effects were independent of the sand bed's PSD. In contrast, the defluidization time increased with increasing gas velocity for all PSDs. Comparing the four PSDs, the narrow and Gaussian distributions had higher defluidization times when using operating temperatures of 700 degrees C and 800 degrees C, gas velocities of 0.163 m/s and 0.187 m/s, and Na concentrations of 0.5% and 0.7%. However, the flat and binary distributions had lower defluidization times under these conditions because they had poor fluidized quality. Thus, the PSD apparently affects the agglomeration and defluidization properties of a sand bed. However, if the system operates at extreme conditions (e.g., high operating temperature, poor mixing and high Na concentration), the PSD's influence on agglomeration will decrease. According to TGA/DTA results, there were two melting points in the agglomerate: 575 degrees C and 782 degrees C. This result confirmed that the liquid-phase eutectic species were formed at the incineration temperature (700-900 degrees C). (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:290 / 295
页数:6
相关论文
共 32 条
[1]   The phenomenology of bed defluidization during the pyrolysis of a food-packaging plastic waste [J].
Arena, U ;
Mastellone, ML .
POWDER TECHNOLOGY, 2001, 120 (1-2) :127-133
[2]   Agglomeration problems during fluidized bed gasification of olive-oil residue: evaluation of fractionation and leaching as pre-treatments [J].
Arvelakis, S ;
Gehrmann, H ;
Beckmann, M ;
Koukios, EG .
FUEL, 2003, 82 (10) :1261-1270
[3]   The relationship between the tendency of lignites to agglomerate and their fusion characteristics in a fluidized bed combustor [J].
Atakül, H ;
Hilmioglu, B ;
Ekinci, E .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (12-13) :1369-1383
[4]  
Chiba S., 1979, POWDER TECHNOL, V22, P225
[5]   Influence of the particle size distribution of powders on the velocities of minimum and complete fluidization [J].
Gauthier, D ;
Zerguerras, S ;
Flamant, G .
CHEMICAL ENGINEERING JOURNAL, 1999, 74 (03) :181-196
[6]  
Gluckman M., 1976, Fluidization Technology, P395
[7]   A criterion for particle agglomeration by collision [J].
He, YH .
POWDER TECHNOLOGY, 1999, 103 (02) :189-193
[8]   Modelling of sintering of iron particles in high-temperature gas fluidisation [J].
Knight, PC ;
Seville, JPK ;
Kamiya, H ;
Horio, M .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (20) :4783-4787
[9]  
Langston B.G., 1960, J METALS, V12, P312
[10]   The effects of agglomeration/defluidization on emission of heavy metals for various fluidized parameters in fluidized-bed incineration [J].
Lin, Chiou-Liang ;
Tsai, Ming-Chih ;
Chang, Chih-Hung .
FUEL PROCESSING TECHNOLOGY, 2010, 91 (01) :52-61