Effect of Vent Area on Dynamic Characteristics of Premixed Methane/Air Explosions in End-vented Channels with Different Length/Diameter Ratios

被引:2
作者
Zhang, Qiang [1 ,2 ]
Chen, Guohua [1 ,2 ,4 ]
Huang, Xianjia [3 ]
Xu, Qiming [1 ,2 ]
Xie, Mulin [1 ,2 ]
Ma, Jiajun [1 ,2 ]
机构
[1] South China Univ Technol, Inst Safety Sci & Engn, Guangzhou, Peoples R China
[2] Guangdong Prov Sci & Technol Collaborat Innovat Ct, Guangzhou, Peoples R China
[3] Guangzhou Inst Ind Technol, Joint Lab Nucl Power Plant Fire Safety, Guangzhou, Peoples R China
[4] South China Univ Technol, Inst Safety Sci & Engn, 381, Wushan Rd, Guangzhou 510640, Peoples R China
基金
中国国家自然科学基金;
关键词
Premixed methane-air; End-vented channels; Explosion overpressure; Length; diameter ratio; Vent area; Distorted tulip flame; HYDROGEN/AIR FLAME PROPAGATION; TULIP FLAME; IGNITION POSITION; DEFLAGRATION; PRESSURE; MIXTURES; BEHAVIOR; FRONT; SIZE; FLOW;
D O I
10.1080/00102202.2023.2189518
中图分类号
O414.1 [热力学];
学科分类号
摘要
Further elucidate the interaction mechanism of pressure-flame-wall in channels under the effects of length/diameter ratio (L/D) and vent area, which helps to propose more effective decompression means. Experiments of premixed methane-air explosions in end-vented channels with L/D of 10, 15 and 20 were conducted under initial conditions (301 +/- 2 K and 1 atm). The results demonstrate that L/D and vent area are critical external factors causing tulip flames and distorted tulip flames. When the vent area is 60 mm x 60 mm similar to 40 mm x 40 mm, the distorted tulip flame can be generated at L/D of 20. Notably, the critical intrinsic factor causing distorted tulip flame is the interaction of reflected pressure waves-flame. It is deduced that flames stagnate or decelerate during the initial stages of irregular flames because rarefaction waves attenuate the driving force of flames. The new overpressure peaks (P-tulip, Pdis-tulip, and Pirr-tulip) induced by tulip flames, distorted tulip flames and irregular tulip flames are identified. Moreover, the drop size and drop ratio of the maximum overpressure decrease with increasing L/D.
引用
收藏
页码:3629 / 3651
页数:23
相关论文
共 52 条
  • [1] Flame deflagration in side-on vented detonation tubes: A large scale study
    Ajrash, Mohammed J.
    Zanganeh, Jafar
    Moghtaderi, Behdad
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2018, 345 : 38 - 47
  • [2] A comparison between end-vented and side-vented gas explosions in large L/D vessels
    Alexiou, A
    Andrews, GE
    Phylaktou, H
    [J]. PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 1997, 75 (B1) : 9 - 13
  • [3] Effect of hydrogen concentration on vented explosion overpressures from lean hydrogen-air deflagrations
    Bauwens, C. R.
    Chao, J.
    Dorofeev, S. B.
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (22) : 17599 - 17605
  • [4] Gas explosion handbook
    Bjerketvedt, D
    Bakke, JR
    vanWingerden, K
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 1997, 52 (01) : 1 - 150
  • [5] Flame acceleration in the early stages of burning in tubes
    Bychkov, Vitaly
    Akkerman, V'yacheslav
    Fru, Gordon
    Petchenko, Arkady
    Eriksson, Lars-Erik
    [J]. COMBUSTION AND FLAME, 2007, 150 (04) : 263 - 276
  • [6] High-speed photography and background oriented schlieren techniques for characterizing tulip flame
    Choudhury, Siba Prasad
    Joarder, Ratan
    [J]. COMBUSTION AND FLAME, 2022, 245
  • [7] On the ''tulip flame'' phenomenon
    Clanet, C
    Searby, G
    [J]. COMBUSTION AND FLAME, 1996, 105 (1-2) : 225 - 238
  • [8] ON THE MECHANISMS OF PRESSURE GENERATION IN VENTED EXPLOSIONS
    COOPER, MG
    FAIRWEATHER, M
    TITE, JP
    [J]. COMBUSTION AND FLAME, 1986, 65 (01) : 1 - 14
  • [9] Statistical analysis of methane explosions in Turkey's underground coal mines and some recommendations for the prevention of these accidents: 2010-2017
    Dursun, Arif Emre
    [J]. NATURAL HAZARDS, 2020, 104 (01) : 329 - 351
  • [10] Vent burst pressure effects on vented gas explosion reduced pressure
    Fakandu, Bala M.
    Andrews, Gordon E.
    Phylaktou, Herodotus N.
    [J]. JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2015, 36 : 431 - 440