Effect of Particle Size on Carbon Nanotube Aggregates Behavior in Dilute Phase of a Fluidized Bed

被引:15
|
作者
Kim, Sung Won [1 ]
机构
[1] Korea Natl Univ Transportat, Sch Chem & Mat Engn, Chungju Si 27469, Chungbuk, South Korea
基金
新加坡国家研究基金会;
关键词
carbon nanotube; fluidized bed; aggregates; particle size; laser sheet technique; HEAT-TRANSFER; SOLIDS;
D O I
10.3390/pr6080121
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluidized bed reactors have been increasingly applied for mass production of Carbon Nanotube (CNT) using catalytic chemical vapor deposition technology. Effect of particle size (d(p) = 131 m and 220 m) on fluidization characteristics and aggregation behavior of the CNT particles have been determined in a fluidized bed for its design and scale-up. The CNT aggregation properties such as size and shape were measured in the dilute phase of a fluidized bed (0.15 m-ID x 2.6 m high) by the laser sheet technique for the visualization. Two CNT particle beds showed different tendency in variations of the aggregates factors with gas velocity due to differences in factors contributing to the aggregate formation. The CNT particles with a larger mean size presented as relatively larger in the aggregate size than the smaller CNT particles at given gas velocities. The aggregates from the large CNT particles showed a sharp increase in the aspect ratio and rapid decrease in the roundness and the solidity with gas velocity. A possible mechanism of aggregates formation was proposed based on the variations of aggregates properties with gas velocity. The obtained Heywood diameters of aggregates have been firstly correlated with the experimental parameter.
引用
收藏
页数:12
相关论文
共 50 条
  • [41] The Effect of Particle Concentration on Bed Particle Diffusion in Dilute Flows
    Moreno-Casas, Patricio A.
    Pablo Toro, Juan
    Sepulveda, Sebastian
    Antonio Abell, Jose
    Gonzalez, Eduardo
    Paik, Joongcheol
    WATER, 2022, 14 (19)
  • [42] Experimental Study on the Effect of Bed Material Amount and Fuel Particle Size on Load Change of Circulating Fluidized Bed
    Tang, Zihua
    Song, Guoliang
    Jiang, Yu
    Yang, Xueting
    Ji, Zengcai
    Sun, Liwei
    JOURNAL OF THERMAL SCIENCE, 2023, 32 (05) : 1758 - 1770
  • [43] Experimental Study on the Effect of Bed Material Amount and Fuel Particle Size on Load Change of Circulating Fluidized Bed
    Zihua Tang
    Guoliang Song
    Yu Jiang
    Xueting Yang
    Zengcai Ji
    Liwei Sun
    Journal of Thermal Science, 2023, 32 : 1758 - 1770
  • [44] Particle size monitoring in a fluidized bed using pressure fluctuations
    Davies, Clive E.
    Carroll, Alison
    Flemmer, Rory
    POWDER TECHNOLOGY, 2008, 180 (03) : 307 - 311
  • [45] Influence of Particle Size on Vacuum-Fluidized Bed Drying
    Kozanoglu, B.
    Martinez, J.
    Alvarez, S.
    Guerrero-Beltran, J. A.
    Welti-Chanes, J.
    DRYING TECHNOLOGY, 2012, 30 (02) : 138 - 145
  • [46] PARTICLE-SIZE EFFECTS IN FLUIDIZED-BED COMBUSTION
    GOLAN, LP
    CHERRINGTON, DC
    DIENER, R
    SCARBOROUGH, CE
    WEINER, SC
    CHEMICAL ENGINEERING PROGRESS, 1979, 75 (07) : 63 - 72
  • [47] Experimental Study on the Effect of Bed Material Amount and Fuel Particle Size on Load Change of Circulating Fluidized Bed
    TANG Zihua
    SONG Guoliang
    JIANG Yu
    YANG Xueting
    JI Zengcai
    SUN Liwei
    JournalofThermalScience, 2023, 32 (05) : 1758 - 1770
  • [48] PARTICLE-SIZE DISTRIBUTION IN A FLUIDIZED-BED REACTOR
    CHEN, TP
    SAXENA, SC
    POWDER TECHNOLOGY, 1976, 15 (02) : 283 - 285
  • [49] Discrete particle simulation of size segregation of particle mixtures in a gas fluidized bed
    Feng, YQ
    Yu, AB
    Circulating Fluidized Bed Technology VIII, 2005, : 268 - 274