Application of the Force Balance Model and Fractal Scaling Analysis for Size Estimation of the Complex-Agglomerates in a Conical Fluidized Bed

被引:0
|
作者
Bahramian, Ali Reza [1 ]
机构
[1] Hamedan Univ Technol, Chem Engn Dept, POB 65155, Hamadan, Hamadan, Iran
基金
美国国家科学基金会;
关键词
Fluidization; Size estimation; Nanoparticle agglomerates; Force balance model; Fractal scaling analysis; PARTICLE FLUIDIZATION; NANOPARTICLES; HYDRODYNAMICS; BEHAVIOR;
D O I
10.30492/IJCCE.2020.38038
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The size estimating of fluidized Titania agglomerates in a conical fluidized bed was studied by force balance model and fractal scaling analysis. The primary size of titania Nano Particles (NPs) was 21 nm, while for complex agglomerates was in the size range of several hundred micrometers. The formation mechanism of simple-agglomerate and complex-agglomerate structures was studied experimentally. The size distribution and morphology of agglomerates were determined by advanced laser dynamic imaging and scanning electron microscopy. The AFM-nanoindentation test was used to determine the elastic modulus of agglomerates with porous structures. The size distribution of Titania NP agglomerates was estimated by the fractal analysis through the relationship between the number of particles and gyration diameter. The fractal exponent obtained from the power-law scaling of agglomerates and the complex agglomerate sizes were determined experimentally and theoretically. A simple theoretical model was applied to estimate the complex agglomerates' size based on the equilibrium of the separation and cohesion forces. The proposed model showed satisfactory results compared with the experimental data. The results of the present study can help to determine the critical gas velocity in achieving the desired agglomerate size of Titania NPs.
引用
收藏
页码:955 / 970
页数:16
相关论文
共 1 条
  • [1] ANALYSIS OF COMPLEX-REACTION SCHEMES IN A FLUIDIZED-BED - APPLICATION OF THE KUNII-LEVENSPIEL MODEL
    IRANI, RK
    KULKARNI, BD
    DORAISWAMY, LK
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (01): : 24 - 30