Simulation of Coal Ash Particle Deposition Experiments

被引:47
作者
Ai, Weiguo [1 ,2 ]
Kuhlman, John M. [1 ,2 ]
机构
[1] Natl Energy Technol Lab, Morgantown, WV 26507 USA
[2] W Virginia Univ, Dept Mech & Aerosp Engn, Morgantown, WV 26506 USA
关键词
THERMOPHORETIC DEPOSITION; VISCOSITY; ADHESION; SURFACE;
D O I
10.1021/ef101294f
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Existing experimental ash particle deposition measurements from the literature have been simulated using the computational fluid dynamics (CFD) discrete phase model (DPM) Lagrangian particle tracking method and an existing ash particle deposition model based on the Johnson-Kendall-Roberts (JKR) theory, in the Fluent commercial CFD code. The experimental heating tube was developed to simulate ash temperature histories in a gasifier; ash-heating temperatures ranged from 1873 to 1573 K, spanning the ash-melting temperature. The present simulations used the realizable k-epsilon turbulence model to compute the gas flow field and the heat transfer to a cooled steel particle impact probe and DPM particle tracking for the particle trajectories and temperatures. A user-defined function (UDF) was developed to describe particle sticking/rebounding and particle detachment on the impinged wall surface. Expressions for the ash particle Young's modulus in the model, E, versus the particle temperature and diameter were developed by fitting to the E values that were required to match the experimental ash sticking efficiencies from several particle size cuts and ash-heating temperatures for a Japanese bituminous coal. A UDF that implemented the developed stiffness parameter equations was then used to predict the particle sticking efficiency, impact efficiency, and capture efficiency for the entire ash-heating temperature range. Frequency histogram comparisons of adhesion and rebound behavior by particle size between model and experiments showed good agreement for each of the four ash-heating temperatures. However, to apply the present particle deposition model to other coals, a similar validation process would be necessary to develop the effective Young's modulus versus the particle diameter and temperature correlation for each new coal.
引用
收藏
页码:708 / 718
页数:11
相关论文
共 16 条
  • [1] Ai WG, 2009, THESIS BRIGHAM YOUNG
  • [2] THERMOPHORETIC DEPOSITION OF PARTICLES IN GAS FLOWING OVER COLD SURFACES
    BATCHELOR, GK
    SHEN, C
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1985, 107 (01) : 21 - 37
  • [3] A MATHEMATICAL-MODEL OF THE IMPACT AND ADHESION OF MICROSPHERES
    BRACH, RM
    DUNN, PF
    [J]. AEROSOL SCIENCE AND TECHNOLOGY, 1992, 16 (01) : 51 - 64
  • [4] An empirical method for the prediction of coal ash slag viscosity
    Browning, GJ
    Bryant, GW
    Hurst, HJ
    Lucas, JA
    Wall, TF
    [J]. ENERGY & FUELS, 2003, 17 (03) : 731 - 737
  • [5] Ichikawa K., 2009, COMMUNICATION
  • [6] Ichikawa K., 2001, P EFF COAL QUAL POW
  • [7] SURFACE ENERGY AND CONTACT OF ELASTIC SOLIDS
    JOHNSON, KL
    KENDALL, K
    ROBERTS, AD
    [J]. PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1971, 324 (1558): : 301 - &
  • [8] Numerical analysis for the thermophoretic coagulation of monodisperse particles at continuum regime
    Jung, Haesung
    Lee, Sun Young
    Kim, Jung Hyeun
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2010, 349 (01) : 438 - 441
  • [9] Kalmanovitch D. P., 1988, P ENG FDN C MIN MATT
  • [10] Losurdo M., 2009, THESIS DELFT U TECHN