Simulations of vented dust explosions in a 5 m3 vessel

被引:23
|
作者
Tascon, Alberto [1 ]
Aguado, Pedro J. [2 ]
机构
[1] Univ La Rioja, Dept Agr & Alimentac, Av Madre de Dios 51, Logrono 26006, Spain
[2] Univ Leon, ESTI Agr, Dept Ingn & Ciencias Agr, Av Portugal 41, E-24071 Leon, Spain
关键词
Dust explosion; Venting; CFD; Numerical modelling; Sensitivity analysis; PROCESS INDUSTRIES; PROPAGATION; PARAMETERS; PRESSURE; SILO; OVERPRESSURES; CONSEQUENCES; MECHANISMS; PREVENTION; TURBULENCE;
D O I
10.1016/j.powtec.2017.08.047
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Vented dust explosions were simulated using the computational fluid dynamics code FLACS-DustEx. The results were compared with previously reported experimental tests performed with maize starch in a 5.2 m(3) vessel with a length/diameter ratio equal to 1.05 using three different vent areas. In addition, a sensitivity study was conducted with respect to some of the parameters involved in the numerical simulations, including dust/air mixture reactivity, grid resolution and area size and activation pressure of the venting device. The simulation results were generally in good agreement with the experimental values, but the CFD code overpredicted explosion pressures for the scenario with the smallest vent area. The sensitivity analysis indicated that the results were dependent on both grid resolution and mixture reactivity. Further simulations confirmed the influence of the activation pressure of the venting device on the explosion overpressure when the vent area was large in comparison to the volume, i.e. with a low K-v (=V-2/3/A). These simulations made it possible to study scenarios outside the range of validity of current venting standards. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:409 / 418
页数:10
相关论文
共 50 条
  • [21] THE INFLUENCE OF VESSEL VOLUME AND EQUIVALENCE RATIO IN VENTED GAS EXPLOSIONS
    Kasmani, R. M.
    Andrews, G. E.
    Phylaktou, H. N.
    JURNAL TEKNOLOGI, 2011, 56
  • [22] Effect of vent area on the vented methane-air deflagrations in a 1 m3 rectangular vessel with and without obstacles
    Rui, Shengchao
    Wang, Qiao
    Chen, Feng
    Li, Quan
    Guo, Jin
    Wang, Jingui
    Wang, Changjian
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2022, 74
  • [23] The Influence Of Vessel Volume And Equivalence Ratio In Vented Gas Explosions
    Kasmani, R. M.
    Andrews, G. E.
    Phylaktou, H. N.
    CISAP4: 4TH INTERNATIONAL CONFERENCE ON SAFETY & ENVIRONMENT IN PROCESS INDUSTRY, 2010, 19 : 463 - 468
  • [24] Characteristics of vented nano-polymethyl methacrylate dust explosions
    Gao, Wei
    Yu, Jianliang
    Zhang, Xinyan
    Li, Jian
    Wang, Bing
    POWDER TECHNOLOGY, 2015, 283 : 406 - 414
  • [25] Influence of dustiness on small-scale vented dust explosions
    Klippel, Alexander
    Scheid, Marc
    Koperski, January
    Wappler, Mike
    Krause, Ulrich
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2013, 26 (06) : 1433 - 1441
  • [26] EXPLOSION PROPAGATION OF NON-HOMOGENEOUS METHANE-AIR CLOUDS INSIDE AN OBSTRUCTED 50 M3 VENTED VESSEL
    HJERTAGER, BH
    BJORKHAUG, M
    FUHRE, K
    JOURNAL OF HAZARDOUS MATERIALS, 1988, 19 (02) : 139 - 153
  • [27] Modeling of maize starch explosions in a 12 m3 silo
    Zhong, SJ
    Deng, XF
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2000, 13 (3-5) : 299 - 309
  • [28] Experimental investigation into the vented hybrid mixture explosions of lycopodium dust and methane
    Ji, Wentao
    Yu, Jianliang
    Yu, Xiaozhe
    Yan, Xingqing
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2018, 51 : 102 - 111
  • [29] External explosions of vented hydrogen-air deflagrations in a cubic vessel
    Rui, Shengchao
    Wang, Changjian
    Luo, Xinjiao
    Jing, Rulin
    Li, Quan
    FUEL, 2021, 301
  • [30] THE EFFECT OF VENT DUCTS ON THE REDUCED EXPLOSION PRESSURES OF VENTED DUST EXPLOSIONS
    LUNN, G
    CROWHURST, D
    HEY, M
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 1988, 1 (04) : 182 - 196