A fractal approach for interpretation of local instantaneous temperature signals around a horizontal heat transfer tube in a bubbling fluidized bed

被引:28
作者
Karamavruc, AI [1 ]
Clark, NN [1 ]
机构
[1] W VIRGINIA UNIV,DEPT MECH & AEROSP ENGN,MORGANTOWN,WV 26506
关键词
fractals; fluidized beds; bubbling beds; signal analysis; heat transfer tubes;
D O I
10.1016/S0032-5910(96)03222-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Temperature signals measured around a horizontal heat transfer tube in a bubbling fluidized bed have been analyzed using Hurst's rescaled range (R/S) analysis. This analysis estimates and identifies long-term persistence or correlation in measured time series. The Hurst exponent H, which is evaluated from R/S analysis, also provides the local fractal dimension of the time series. A new approach to analyze an air fluidized particle system is proposed based on the evaluation of the Hurst exponent. Two Hurst exponents can be evaluated from a single time series, one from the discrete time fractional noise (where the linearity of the signal is subtracted and short-term fluctuations are emphasized) and the other from the signal itself (without subtracting the linearity of the signal). The authors argue that the Hurst exponent obtained from discrete time fractional noise characterizes the particle motion, whereas the Hurst exponent obtained from the signal itself characterizes the bubble motion. Moreover, a comparison between these two Hurst components identifies the zones where an alternating type of contact between the tube surface and the bubble-emulsion phase occur. The results were interpreted in conjunction with the mutual information function. The mutual information function provides the relationship between the data points separated in time and uses only the statistical relationship between the data points. The mutual information functions and the Hurst exponents exhibited similar trends around the heat transfer tube.
引用
收藏
页码:235 / 244
页数:10
相关论文
共 41 条
  • [1] EXPERIMENTAL INVESTIGATIONS OF CHAOTIC HYDRODYNAMIC ATTRACTORS IN CIRCULATING FLUIDIZED-BEDS
    BOUILLARD, JX
    MILLER, AL
    [J]. POWDER TECHNOLOGY, 1994, 79 (03) : 211 - 215
  • [2] A HEAT-TRANSFER MODEL FOR TUBES IMMERSED IN GAS-FLUIDIZED BEDS
    CHANDRAN, R
    CHEN, JC
    [J]. AICHE JOURNAL, 1985, 31 (02) : 244 - 252
  • [3] DIFFERENTIAL PRESSURE MEASUREMENTS IN A SLUGGING FLUIDIZED-BED
    CLARK, NN
    MCKENZIE, EA
    GAUTAM, M
    [J]. POWDER TECHNOLOGY, 1991, 67 (02) : 187 - 199
  • [4] Cover T. M., 2005, ELEM INF THEORY, DOI 10.1002/047174882X
  • [5] DAW CS, 1993, AICHE SYM S, V89, P103
  • [6] FRACTAL ANALYSIS OF FLUIDIZED PARTICLE BEHAVIOR IN LIQUID-SOLID FLUIDIZED-BEDS
    FAN, LT
    KANG, Y
    NEOGI, D
    YASHIMA, M
    [J]. AICHE JOURNAL, 1993, 39 (03) : 513 - 517
  • [7] PRESSURE-FLUCTUATIONS IN A FLUIDIZED-BED
    FAN, LT
    HO, TC
    HIRAOKA, S
    WALAWENDER, WP
    [J]. AICHE JOURNAL, 1981, 27 (03) : 388 - 396
  • [8] STOCHASTIC-ANALYSIS OF A 3-PHASE FLUIDIZED-BED - FRACTAL APPROACH
    FAN, LT
    NEOGI, D
    YASHIMA, M
    NASSAR, R
    [J]. AICHE JOURNAL, 1990, 36 (10) : 1529 - 1535
  • [9] Feder J., 1988, FRACTALS PLENUM
  • [10] INDEPENDENT COORDINATES FOR STRANGE ATTRACTORS FROM MUTUAL INFORMATION
    FRASER, AM
    SWINNEY, HL
    [J]. PHYSICAL REVIEW A, 1986, 33 (02): : 1134 - 1140