Determination of the explosion parameters of methane-air mixtures as function of the ignition source and the volume and shape of the explosion chambers

被引:4
作者
Alvarez-Fernandez, Martina-Inmaculada [1 ]
Prendes-Gero, Maria-Belen [2 ]
Pola-Alonso, Isaac [3 ]
Conde-Fernandez, Lucia [1 ]
Luengo-Garcia, Juan -Carlos [4 ]
机构
[1] Univ Oviedo, Sch Min Energy & Mat Engn Oviedo, Dept Min Exploitat & Prospecting, Oviedo, Asturias, Spain
[2] Univ Oviedo, Polytech Sch Engn Gijon, Dept Construct & Mfg Engn, Gijon, Asturias, Spain
[3] Govt Principal Asturias, Inst Econ Dev Principal Asturias, Oviedo, Asturias, Spain
[4] Univ Oviedo, Sch Min Energy & Mat Engn Oviedo, Dept Energy, Oviedo, Asturias, Spain
关键词
Methane; Air mixtures; Explosion characteristics; Experimental study; Maximum pressure characteristics; Pressure gradients; Pressure acceleration; FLAMMABILITY LIMIT; DEFLAGRATION; TRANSITION; OBSTACLES; ENERGY; FLAME; FLOW;
D O I
10.1016/j.jlp.2022.104862
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The combination of methane -air can cause potentially explosive mixtures, which in contact with an energy source can ignite, resulting not only in the destruction of infrastructure but also in the death of people. The aim of this paper is to study the ignition of methane -air mixtures with different concentration of methane, as a function of the ignition sources used and the volume and geometry of the explosion chamber. For this purpose, the 'Dynamic Behaviour of the Rock mass (DinRock)' research group of the University of Oviedo has designed and manufactured 3 explosion chambers of different sizes and shapes, instrumented with dynamic pressure sensors and accelerometers. In addition, the ignition process has been recorded with a high-speed camera. With the results obtained after a laboratory-scale experimental campaign, the maximum pressure reached, the pressure gradients and the acceleration of the pressure waves were analysed. Thus, it has been determined that the maximum pressure reached is independent of the ignition source used and the chamber volume, but not of the chamber geometry. Methane (CH4) concentrations between 8.0 and 9.0% generated the highest pressures between 1.5 and 2.5 MPa. A correlation between peak acceleration and peak pressure has also been established allowing to identify whether a deflagration or a detonation has occurred.
引用
收藏
页数:11
相关论文
共 30 条
[1]   Methane-coal dust hybrid fuel explosion properties in a large scale cylindrical explosion chamber [J].
Ajrash, Mohammed Jabbar ;
Zanganeh, Jafar ;
Moghtaderi, Behdad .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2016, 40 :317-328
[2]   Effects of ignition energy on fire and explosion characteristics of dilute hybrid fuel in ventilation air methane [J].
Ajrash, Mohammed Jabbar ;
Zanganeh, Jafar ;
Moghtaderi, Behdad .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2016, 40 :207-216
[3]   Measurements of minimum ignition energy in premixed laminar methane/air flow by using laser induced spark [J].
Beduneau, JL ;
Kim, B ;
Zimmer, L ;
Ikeda, Y .
COMBUSTION AND FLAME, 2003, 132 (04) :653-665
[4]   Coal dust explosibility [J].
Cashdollar, KL .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 1996, 9 (01) :65-76
[5]   Overview of dust explosibility characteristics [J].
Cashdollar, KL .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2000, 13 (3-5) :183-199
[6]  
Chi Ma, 2018, Procedia Engineering, V211, P538, DOI 10.1016/j.proeng.2017.12.046
[7]  
Dhillon B.S., 2010, MINE SAFETY MODERN A, DOI [10.1007/978-1-84996-115-8, DOI 10.1007/978-1-84996-115-8]
[8]   Flame acceleration and DDT in channels with obstacles: Effect of obstacle spacing [J].
Gamezo, Vadim N. ;
Ogawa, Takanobu ;
Oran, Elaine S. .
COMBUSTION AND FLAME, 2008, 155 (1-2) :302-315
[9]   Quantitative structure-property relationship for prediction of the lower flammability limit of pure compounds [J].
Gharagheizi, Farhad .
ENERGY & FUELS, 2008, 22 (05) :3037-3039
[10]   Flammability limit measurements for dusts in 20-L and 1-m3 vessels [J].
Going, JE ;
Chatrathi, K ;
Cashdollar, KL .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2000, 13 (3-5) :209-219