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
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