Multiscale resolution of fluidized-bed pressure fluctuations

被引:139
作者
Zhao, GB [1 ]
Yang, YR [1 ]
机构
[1] Zhejiang Univ, Dept Chem Engn & Biochem Engn, Hangzhou 310027, Peoples R China
关键词
D O I
10.1002/aic.690490407
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pressure fluctuation signals measured from four different axial locations in a bubbling bed 0.3 m in diameter and 3 m in height were analyzed using multiple approaches, including wavelet transform, Hurst analysis, multiscale resolution, and time-delay embedding. After examining decomposition residuals using different compact support Daubechies wavelets, the Daubechies second-order wavelet was chosen as an optimal wavelet for decomposing pressure signals. Hurst analysis of the decomposed signals shows that the measured pressure fluctuations can be resolved to three characteristic scales: bifractal mesoscale signals with two distinct Hurst exponents; monofractal micro- and macroscale signals with only one characteristic Hurst exponent. Energy profiles of the three scale components confirm that the measured pressure signals mainly reflect the mesoscale component. Time-delay embedding analysis of three scale signals demonstrates that the microscale dynamics is more complex than the mesoscale dynamics, and the mesoscale dynamics is more complex than the macroscale dynamics. That this result cannot be found solely from Hurst analysis shows the importance of integrating multiple approaches for characterizing the complexity of fluidized systems.
引用
收藏
页码:869 / 882
页数:14
相关论文
共 62 条
[1]   Characteristics of gas-fluidized beds in different flow regimes [J].
Bai, D ;
Issangya, AS ;
Grace, JR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (03) :803-811
[2]   Flow structure in a fast fluidized bed [J].
Bai, D ;
Shibuya, E ;
Masuda, Y ;
Nakagawa, N ;
Kato, K .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (06) :957-966
[3]   Chaotic behavior of fluidized beds based on pressure and voidage fluctuations [J].
Bai, D ;
Bi, HT ;
Grace, JR .
AICHE JOURNAL, 1997, 43 (05) :1357-1361
[4]   Fractal characteristics of gas-solids flow in a circulating fluidized bed [J].
Bai, D ;
Shibuya, E ;
Nakagawa, N ;
Kato, K .
POWDER TECHNOLOGY, 1997, 90 (03) :205-212
[5]  
BAKSHI BR, 1995, T I CHEM ENG-LOND, V33, P608
[6]   PROPAGATION OF PRESSURE WAVES AND FORCED-OSCILLATIONS IN GAS-SOLID FLUIDIZED-BEDS AND THEIR INFLUENCE ON DIAGNOSTICS OF LOCAL HYDRODYNAMICS [J].
BI, HT ;
GRACE, JR ;
ZHU, J .
POWDER TECHNOLOGY, 1995, 82 (03) :239-253
[7]   Hurst's analysis to detect minimum fluidization and gas maldistribution in fluidized beds [J].
Briens, CL ;
Briens, LA ;
Hay, J ;
Hudson, C ;
Margaritis, A .
AICHE JOURNAL, 1997, 43 (07) :1904-1908
[8]   CHARACTERIZATION OF DILUTE GAS-SOLIDS FLOWS USING THE RESCALED RANGE ANALYSIS [J].
CABREJOS, FJ ;
KLINZING, GE .
POWDER TECHNOLOGY, 1995, 84 (02) :139-156
[9]   EXPERIMENTAL CHARACTERIZATION OF THE SOLID-PHASE CHAOTIC DYNAMICS IN 3-PHASE FLUIDIZATION [J].
CASSANELLO, M ;
LARACHI, F ;
MARIE, MN ;
GUY, C ;
CHAOUKI, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (09) :2971-2980
[10]   COMPUTING THE KOLMOGOROV-ENTROPY FROM TIME SIGNALS OF DISSIPATIVE AND CONSERVATIVE DYNAMICAL-SYSTEMS [J].
COHEN, A ;
PROCACCIA, I .
PHYSICAL REVIEW A, 1985, 31 (03) :1872-1882