期刊文献+

气固流化床中空隙率波动信号的自由度数确定 被引量:2

Determination of the Freedom Degrees of Voidage Fluctuation Signals in Gas-Solid Fluidized Bed
下载PDF
导出
摘要 确定气固流化床体系的自由度数是对该系统进行定量描述的前提和基础。本文采用小波分析方法,将气固流化床中空隙率波动信号进行小波变换,以相空间重构和混沌分析理论为基础,通过G-P算法和Liangyuechao提出的方法计算空隙率波动信号小波系数的最小嵌套维,从而确定了气固流化床中空隙率波动信号的自由度数,并对两种确定最小嵌套维的方法进行了比较。 Determination the number of freedom degree of voidage fluctuation signals in gas- solid fluidized bed is the premise and basis for quantificationally describing the gas- solid fluidized system. In this paper, the voidage fluctuation signals in gas- solid fluidized bed were wavelet-transformed by the wavelet analysis, and the number of freedom degree for voidage fluctuation signals were determined by using G-P method and Liangyuechao method to calculate minimal embedding dimension of wavelet coefficient for voidage fluctuation signals according to the phase-space reconstruction and chaos analysis theories. And the two methods for determining minimal embedding dimension were compared.
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2006年第5期66-69,共4页 Natural Gas Chemical Industry
关键词 气固流化床 空隙率 波动信号 小波变换 自由度数 gas-solid fluidized bed voidage fluctuation signal wavelet transform freedom degree
  • 相关文献

参考文献6

  • 1Daw C S, Lawkins W F, Downing D J. Chaotic characteristics of a complex gas-solid flow[J]. Phy Rev A, At Mol Opt Phys,1990,41(2):1179-1181.
  • 2Cor M Van den Bleek, Jaap C Schouten. Deterministic chaos: a new tool in fluidized bed design and opreation[J]. Chem Eng J, 1993,53:75-87.
  • 3谢应齐 曹杰.非线性动力学数学方法[M].北京:气象出版社,2002..
  • 4P Grassberger, I Procaccia. Characterization of strange attractors[J]. Phys Rev Lett, 1985,57.617-628.
  • 5马军海,陈予恕,刘曾荣.动力系统实测数据的非线性混沌模型重构[J].应用数学和力学,1999,20(11):1128-1134. 被引量:32
  • 6赵贵兵,陈纪忠,阳永荣.Daubechies小波对流化床压力波动的分解研究[J].高校化学工程学报,2003,17(3):272-278. 被引量:25

二级参考文献22

  • 1CHEN Gong(陈珙) WANG Bao-liang(王保良).YANG Jiang(杨江) LI Hai-qing(李海青).Application of wavelets transform to the fuzzy identification of gas-solid two-phase flow regimes(基于小波变换的气液两相流流型模糊辨识)[J].J Chem Eng of Chinese Univ(高校化学工程学报),1999,13(4):303-308.
  • 2Bakshi B R, Zhong H, Jiang P, Fan L S. Analysis of flow in gas-liquid bubble columns using multi-resolution methods [J].Trans IChE, 1995, 73, Part A: 608-614.
  • 3Ran J, Mao Q, Li J, Lin W. Wavelet analysis of dynamic behavior in fluidized beds [J]. Chemical Engineering Science, 2001,56: 981-988.
  • 4Li J, Compromise and resolution--Exploring the multi-scale nature of gas-solid fluidization [J]. Powder Technology, 2000, 111:50-59.
  • 5Lu X, Li H. Wavelet analysis of pressure fluctuation signals in a bubbling fluidized bed [J]. Chemical Engineering Journal,1999, 75:113-119.
  • 6Zhou H, Lu J, Lin L. Turbulence structure of the solid phase in transition region of a circulating fluidized bed [J]. Chemical Engineering Science, 2000, 55: 839-847.
  • 7He Z, Zhang W, He K, Chen B. Modeling pressure fluctuations via correlation structure in a gas-solids fluidized bed [J]. AIChE J, 1997, 43(7): 1914-1920.
  • 8Daubechies I. Orthonormal bases of compactly supported wavelets [J]. Comm Pure Appl Math, 1988, 41 : 909-996.
  • 9Mallat S. A theory for multiresolution signal decomposition: the wavelet representation [J]. IEEE Trans Pattern Anal Mach Intell, 1989, 11(7): 674-693.
  • 10云南省社会科学院嫡.走向21世纪的云南民族文化[C].云南人民出版社,1999..

共引文献57

同被引文献23

  • 1ZHANG W, Tung Y, Johnson F. Radial voidage profiles in fast fluidized beds of different diameters [J]. Chem Eng Sci, 1991,46(12): 3045-3052.
  • 2Gungor A, Eskin N. Hydrodynamic modeling of a circulating fluidized bed [J]. Powder Technology, 2007, 172(1): 1-13.
  • 3WU Bang-you, YU Guang, Bellehumeur C et al. Dynamic flow behavior measurements in gas-solid fluidized beds using different non-intrusive techniques and polyethylene powder [J]. Flow Measurement and Instrumentation, 007, 18(5-6): 197-203.
  • 4Kozanoglu B, Chanes J, Cuautle D et al. Hydrodynamics of large particle fluidization in reduced pressure operations: an experimental study [J]. Powder Technology, 2002, 125 (1): 55-60
  • 5Kupiers J, Tammes H, Princs W. Experimental and theoretical porosity profiles in two dimensional gas-fluidized bed with a central jet [J]. Powder Technology, 1992, 71(1): 87-99.
  • 6Kunii D. Levenspiel O. Fluidization Engineering (Second edition) [M]. Boston: Butter-Heinemann, 1991, 15.
  • 7Taghipour F, Ellis N, Wong C. Experimental and computational study of gas-solid fluidized bed hydrodynamics [J]. Chem Eng Sci, 2005, 60(24): 6857-6867.
  • 8Issangya A, Grace J, Bai D et al. Radial voidage variation in CFB risers [J]. Canadian Journal of Chemical Engineering, 2001, 79(2): 279-286.
  • 9Xu Guang-wen, Sun Guo-gang, Gao Shi-qiu. Estimating radial voidage profiles for all fluidization regimes in circulating fluidized bed risers [J]. Powder Technoiogy, 2004, 139(2): 186-192.
  • 10漆小波,张辉,黄卫星,祝京旭.下行气固两相流充分发展段的颗粒浓度[J].高校化学工程学报,2007,21(4):621-626. 被引量:2

引证文献2

二级引证文献13

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部