期刊文献+

Charge transfer and bipolar charging of particles in a bubbling fluidized bed

原文传递
导出
摘要 Particle-particle and particle-wall collisions in gas-solid fluidized beds lead to charge accumulation on particles.This work evaluated the effect of fluidization time on charge transfer and bipolar charging(charge separation)and their influence on hydrodynamic structures in a fluidized bed.Experiments were performed with glass beads and polyethylene particles in a glass column.The pressure fluctuations and net electrostatic charge of particles were measured during fluidization.Wavelet and short-time Fourier transforms were used to analyze pressure fluctuations.The results revealed that bipolar charging is the dominant tribocharging mechanism in a bed of glass beads.Bipolar charging in a bed of particles with a narrow size distribution does not affect either hydrodynamic structures or the transition velocity to the turbulent regime.A large difference between the work functions of the wall and particle in the bed of polyethylene particles leads to high charge transfer.Formation of a stagnant particle layer on the wall eventually causes the energy of macro-structures to increase to its maximum.At longer fluidization times,the macro-structural energy decreases and bubbles shrink until the electrostatic charge reaches the equilibrium level.These results well describe the effect of fluidization time on hydrodynamic structures.
出处 《Particuology》 SCIE EI CAS CSCD 2021年第1期109-115,共7页 颗粒学报(英文版)
  • 相关文献

参考文献3

二级参考文献72

  • 1Abbasi, M., Sotudeh-Gharebagh, R., Mostoufi, N., & Mahjoob, M. J. (2009). Non-intrusive monitoring of bubbles in a gas-solid fluidized bed using vibration signature analysis. Powder Technology, 196,278-285.
  • 2Babaei, B., Zarghami, R., Sedighikamal, H., Sotudeh-Gharebagh, R., & Mostoufi, N. (2012). Investigating the hydrodynamics of gas-solid bubbling fluidization using recurrence plot. Advanced Powder Technology, 23(3), 380-386.
  • 3Briongos, J. V., & Guardiola, J. (2005). New methodology for scaling hydrodynamic data from a 2D-fiuidized bed. Chemical Engineering Science, 60(18), 5151-5163.
  • 4Briongos, J. V., Aragon, J. M., & Palancar, M. C. (2007). Phase space structure and multiresolution analysis of gas-solid fluidized bed hydrodynamics: Part II: Dynamic analysis. Chemical Engineering Science, 62( 11), 2865-2879.
  • 5Chen, R. C., & Fan, L.-S. (1992). Particle image velocimetry for characterizing the flow structure in three-dimensional gas-liquid-solid fluidized beds. Chemical Engineering Science, 47(13-14), 3615-3622.
  • 6Croxford, A. J., Harrison, A. J. L., & Gilbertson, M. A. (2005). The optimisation of pressure measurements for the control of bubbling fluidised bed s. Journal of Chemical Reactor Engineering, 3, A39.
  • 7Daw, C. S., & Halow, J. S. (1991). Characterization of voidage and pressure signals from fluidized bed using deterministic chaos theory. In E.J. Anthony (Ed.), Proceedings of the 11th International Conference on Fluidized Bed Combustion (pp. 777-786). New York: ASME.
  • 8Eckmann, J. P., Kamphorst, S. O., 8i Ruelle, D. (1987). Recurrence plots of dynamical systems. Europhysics Letters, 4,973-977.
  • 9Gandhi, A. B., Joshi, J. B., Kulkarni, A. A., Jayaraman, V. K., & Kulkarni, B. D. (2008). SVR-based prediction of point gas hold-up for bubble column reactor through recurrence quantification analysis of LDA time-series. International Journal of Multiphase How, 34,1099-1107.
  • 10Geidart, D. (1973). Types of gas fluidization. Powder Technology., 7(5), 285-292.

共引文献26

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