On the pyrotechnic ignitors role in dust explosion testing: Comparison between 20 L and 1 m3 explosion vessels

被引:15
|
作者
Portarapillo, Maria [1 ]
Sanchirico, Roberto [2 ]
Di Benedetto, Almerinda [1 ]
机构
[1] Univ Naples Federico II, Dept Chem Mat & Prod Engn, I-80125 Naples, Italy
[2] CNR, STEMS, Ist Sci & Tecnol Energia Mobilita Sostenibill, Naples, Italy
关键词
1  m(3) vessel; CFD simulation; overdriving phenomenon; pyrotechnic ignitors effect; Siwek sphere; TURBULENT FLUID-FLOW; CFD SIMULATIONS; DISPERSION; IGNITION;
D O I
10.1002/prs.12249
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Several phenomena (e.g., initial turbulence level, overdriving, underdriving, etc.) affect the measurement of dust explosion parameters in the 20 L and 1 m(3) standard test vessels. Estimating the role of each phenomenon is crucial to understand the discrepancies observed over the years between the data collected using these vessels. In this work, we focus on the role of the pyrotechnic ignitors on the pressure trend and the temperature distribution. We run explosion tests in the 20 L vessel to measure the pressure-time history generated by the explosion of pyrotechnic ignitors. Moreover, we performed CFD simulations to simulate the spatial/temporal evolution of the temperature map from the hot core due to the igniter explosion toward the vessel walls. The explosion of the pyrotechnic ignitors shows a significant increase of pressure in the 20 L vessel, suggesting that flame propagation is occurring inside the vessel. Furthermore, the localized increase of temperature due to the ignitor explosions, diffuse, and then uniformize much more rapidly in the 20 L vessel than in the 1 m(3) vessel. The flame propagation generated by the ignitors is very relevant in the 20 L sphere leading to the overdriving phenomenon. This result justifies the fact that for many organic dusts, the deflagration index values measured in the 20 L are much higher than those measured in the 1 m(3) vessel. CFD simulations show that the hot core generated by the ignitors dissipate much faster in the 20 L vessel than in the 1 m(3) vessel, due to the higher turbulence level of the smaller vessel. Therefore, dusts whose combustion is controlled by particle heating are more prone to sustain combustion in the 1 m(3) than in the 20 L vessel.
引用
收藏
页码:289 / 295
页数:7
相关论文
共 21 条
  • [1] CFD simulations of dust dispersion in the 1 m3 explosion vessel
    Portarapillo, Maria
    Trofa, Marco
    Sanchirico, Roberto
    Di Benedetto, Almerinda
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2020, 68
  • [2] Comparison of the explosion characteristics and flame speeds of pulverised coals and biomass in the ISO standard 1 m3 dust explosion equipment
    Medina, Clara Huescar
    MacCoitir, Brian
    Sattar, Hamed
    Slatter, David J. F.
    Phylaktou, Herodotos N.
    Andrews, Gordon E.
    Gibbs, Bernard M.
    FUEL, 2015, 151 : 91 - 101
  • [3] Explosion Parameters of Coke Oven Gas in 1 m3 Explosion Chamber
    Skrinsky, Jan
    Veres, Jan
    Peer, Vaclav
    Friedel, Pavel
    Travnickova, Jana
    Dalecka, Andrea
    CISAP7: 7TH INTERNATIONAL CONFERENCE ON SAFETY & ENVIRONMENT IN PROCESS INDUSTRY, 2016, 53 : 7 - 12
  • [4] Construction of a 36 L dust explosion apparatus and turbulence flow field comparison with a standard 20 L dust explosion vessel
    Castellanos, Diana
    Carreto, Victor
    Skjold, Trygve
    Yuan, Shuai
    Chaudhari, Purvali
    Mannan, M. Sam
    Mashuga, Chad
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2018, 55 : 113 - 123
  • [5] Effect of turbulence spatial distribution on the deflagration index: Comparison between 20 L and 1 m3 vessels
    Portarapillo, Maria
    Sanchirico, Roberto
    Di Benedetto, Almerinda
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2021, 71
  • [6] Experimental and numerical simulation study on the effect of ignition delay time on dust explosion in the 1 m3 vessel
    Ren, Jiafan
    Chang, Chongye
    Rao, Guoning
    Bai, Chunhua
    Jing, Qi
    Peng, Xu
    Xiao, Qiuping
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2022, 78
  • [7] A vented corn starch dust explosion in an 11.5 m3 vessel: Experimental and numerical study
    Huang, Chen
    Bloching, Marius
    Lipatnikov, Andrei N.
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2022, 75
  • [8] Combustion and Explosion Characteristics of Pulverised Wood, Valorized with Mild Pyrolysis in Pilot Scale Installation, Using the Modified ISO 1 m3 Dust Explosion Vessel
    Saeed, Muhammad Azam
    Niedzwiecki, Lukasz
    Arshad, Muhammad Yousaf
    Skrinsky, Jan
    Andrews, Gordon E.
    Phylaktou, Herodotos N.
    APPLIED SCIENCES-BASEL, 2022, 12 (24):
  • [9] Turbulent Flames Speeds and Laminar Burning Velocities of Dusts using the ISO 1 m3 Dust Explosion Method
    Sattar, Hamed
    Andrews, Gordon E.
    Phylaktou, Herodotos N.
    Gibbs, Bernard M.
    CISAP6: 6TH INTERNATIONAL CONFERENCE ON SAFETY & ENVIRONMENT IN PROCESS & POWER INDUSTRY, 2014, 36 : 157 - 162
  • [10] CFD simulation of turbulent fluid flow and dust dispersion in the 1 m3 explosion vessel equipped with the rebound nozzle
    Portarapillo, Maria
    Trofa, Marco
    Sanchirico, Roberto
    Di Benedetto, Almerinda
    JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2022, 76