EXPERIMENTAL STUDY ON FLAME PROPAGATION IN A STRAIGHT PIPE
DOI:
https://doi.org/10.11113/jt.v78.9568Keywords:
Overpressure, fast flame, reflection wave, closed straight pipe, end pipeAbstract
Flame propagation in a closed pipe with diameter 0.1 m and 5.1 m long, as well as length to diameter ratio (L/D) of 51, was studied experimentally. Hydrogen/air, acetylene/air and methane/air with stoichiometric concentration were used to observe the trend of flame propagation throughout the pipe. Experimental work was carried out at operating condition: pressure 1 atm and temperature 273 K. Results showed that all fuels are having a consistent trend of flame propagation in one-half of the total pipe length in which the acceleration is due to the piston-like effect. Beyond the point, fuel reactivity and tulip phenomenon were considered to lead the flame being quenched and decrease the overpressures drastically. The maximum overpressure for all fuels are approximately 1.5, 7, 8.5 barg for methane, hydrogen, and acetylene indicating that acetylene explosion is more severe.Â
References
M. A. Liberman, M. F. Ivanov, A. D. Kiverin, M. S. Kuznetsov, A. A. Chukalovsky, and T. V. Rakhimova. 2010. Acta Astronautica. 67: 688-701.
D. Bradley, M. Lawes, and K. Liu. 2008. Combustion and Flame. 154: 96-108.
V. N. Gamezo, T. Ogawa, and E.S. Oran. 2008. Combustion and Flame. 155: 302-315.
G. Ciccarelli, and S. Dorofeev. 2008. Progress in Energy and Combustion Science. 34: 499-550.
R. K. Zipf Jr, V. N. Gamezo, K. M. Mohamed, E. S. Oran, and D.A. Kessler. 2014. Combustion and Flame. 161: 2165-2176.
M. Wu, M. P. Burke, S. F. Son, and R. A. Yetter. 2007. Proceedings of the Combustion Institute. 31: 2429-2436.
R. Blanchard, D. Arndt, R. Grätz, and S. Scheider. 2011. Journal of Loss Prevention in the Process Industries. 24: 194-199.
C. Zhu, B. Lin, and B. Jiang. 2012. Journal of Loss Prevention in the Process Industries. 25: 383-390.
G.Thomas, R. Bambrey, and C. Brown. 2001. Combustion Theory Model. 5: 573–594.
H. Phylaktou, M. Foley, and G.E. Andrews. 1993. Journal of Loss Prevention in the Process Industries. 6: 21-29.
[11] G.Thomas,, G. Oakley, and R. Bambrey. 2010. Process Safety and Environmental Protection. 88: 75-90.
J. Li, W. Lai, K. Chung, and F. Lu. 2005. Shock Waves. 14: 413-420.
E. S. Oran, J. D. Otto, and J. D. Anderson. 2001. American Physical Society, 54th Annual Meeting of the Division of Fluid Dynamics San Diego, California
R. J. Harris. 1983. The Investigation And Control Of Gas Explosions In Building And Heating Plant., New York: E&F N Spon Ltd.
D. Bradley, T.M. Cresswell, and J.S. Puttock. 2001. Combustion and Flame. 124: 551-559.
A.K.Oppenheim. 1985. Philosophical Transactions of the Royal Society of London. Series A, Mathematical and Physical Sciences. 315: 471-508.
B. Jiang, . 2013. Journal of Loss Prevention in the Process Industries. 26: 782-791.
H. Xiao, D. Makarov, J. Sun, and V. Molkov. 2012. Combustion and Flame. 159: 1523-1538.
B. Zhou, A. Sobiesiak, and P. Quan. 2006. International Journal of Thermal Sciences. 45: 457-474.
V. Bakić, S. Nemoda, M. SijerÄić, V. Turanjanin, and B. Stanković. 2006. International Journal of Heat and Mass Transfer. 49: 4023-4032.
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