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气/液-固两相流中的粒子速度 被引量:1

Particle velocity in gas/liquid-solid two-phase flow
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摘要 通过实验研究和理论分析,考察了提升管中颗粒相的质量守恒;发现在传统的两相流研究中,对颗粒速度的时间平均和算术平均存在着误用。在传统理论中,由于引入了颗粒相的体积分率项,实际上是对离散的颗粒进行了连续化的假设。由此不可避免地造成颗粒速度时间平均和算术平均的混淆。在微观尺度上对气/液-固两相流中颗粒速度时间平均的物理意义进行了分析,给出了计算非连续流场中颗粒时均速度的表达式,并提出了分析颗粒相质量守恒的方法。 Gas/liquid-solid two-phase flow is ubiquitous in chemical engineering.This paper theoretically and experimentally analyzes the mass conservation of solid phase in a CFB riser.It is revealed that the time-average particle velocity and arithmetical-average particle velocity are misused in the traditional viewpoint of two-phase flow.The introduction of solid volume fraction in a two-phase flow actually denotes an assumption that the discrete particles are treated as a continuum.Then the misuse of time-average particle velocity and arithmetical-averaging appears inevitable.The physical meaning of time-average particle velocity in a gas/liquid-solid two-phase flow is discussed on a microcosmic scale.An equation for computing the time-average particle velocity in a discrete two-phase flow is given.Furthermore,a proper approach is proposed to analyze the mass conservation of discrete particles.
出处 《化工学报》 EI CAS CSCD 北大核心 2010年第9期2217-2224,共8页 CIESC Journal
基金 国家自然科学基金项目(20776155)~~
关键词 两相流 颗粒速度 质量守恒 时间平均 算术平均 two-phase flow particle velocity mass conservation time-average arithmetical-average
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  • 1Yan A, Ball J, Zhu J. Scale up effect of riser reactor (3) axial and radial solid flux distribution and flow development. Chemical Engineering Journal, 2005, 109:97-106.
  • 2Zhang H, Huang W, Zhu J. Gas-solid flow behavior: CFB riser vs. downer. AIChE Journal, 2001, 47 : 2000-2011.
  • 3Issangya A, Grace J, Bai D, Zhu J. Further measurement of flow dynamics in a high-density circulating fluidized bed riser. Powder Technology, 2000, 111:104-113.
  • 4Issangya A, van Meer E, Davidson J, Thorpe R. Gas-solid flow in the diffuser of a circulating fluidized bed riser. Powder Technology, 2000, 111:94 -103.
  • 5Issangya A. Flow dynamics in high density circulating fluidized beds[D]. Vaneouver: University of British Columbia, 1998.
  • 6Issangya A, Bai D, Bi H, Lira K, Zhu J, Grace J. Suspension densities in a high-density circulating fluidized bed riser. Chemical Engineering Science, 1999, 54: 5451-5460.
  • 7Wei F, Lin H, Cheng Y, Wang Z, Jin Y. Profiles of particle velocity and solid fraction in a high-density riser. Powder Technology, 1998, 100:183-189.
  • 8Wei F, Lu F, Jin Y, Yu Z. Mass flux profiles in high density circulating fluidized bed. Powder Technology, 1997, 91: 189- 195.
  • 9Liu J. Particle and gas dynamics of high density circulating fluidized bed[D]. Vancouver: University of British Columbia, 2001.
  • 10Liu J, Grace J, Bi X. Novel multifunctional optical fiber probe (Ⅰ), Development and validation. AIChE Journal, 2003,49: 1405-1420.

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