A correlation of the lower flammability limit for hybrid mixtures

Abstract Hybrid mixtures are widely encountered in industries such as coal mines, paint factories, pharmaceutical industries, or grain elevators. Hybrid mixtures explosions involving dust and gas can cause great loss of lives and properties. The lower flammability limit (LFL) is a critical parameter when conducting a hazard assessment or developing mitigation methods for processes involving hybrid mixtures. Unlike unitary dust or gas explosions, which have been widely studied in past decades, only minimal research focuses on hybrid mixtures, and data concerning hybrid mixtures can rarely be found. Although methods to predict the LFL have been developed by using either Le Chatelier's Law, which was initially proposed for homogeneous gas mixtures, or the Bartknecht curve, which was adopted for only certain hybrid mixtures, significant deviations still remain. A more accurate correlation to predict an LFL for a hybrid mixtures explosion is necessary for risk assessment. This work focuses on the study of hybrid mixtures explosions in a 36 L dust explosion apparatus including mixtures of methane/niacin, methane/cornstarch, ethane/niacin and ethylene/niacin in air. By utilizing basic characteristics of unitary dust or gas explosions, a new formula is proposed to improve the prediction of the LFL of the mixture. The new formula is consistent with Le Chatelier's Law.

[1]  Rolf K. Eckhoff,et al.  Dust explosion causation, prevention and mitigation: An overview , 2010 .

[2]  M. Mannan,et al.  Experimental measurement and numerical analysis of binary hydrocarbon mixture flammability limits , 2009 .

[3]  Paola Russo,et al.  Prevention and mitigation of dust and hybrid mixture explosions , 2010 .

[4]  A. Denkevits Explosibility of hydrogen–graphite dust hybrid mixtures , 2007 .

[5]  R. Prugh The relationship between flash point and LFL with application to hybrid mixtures , 2008 .

[6]  Rolf K. Eckhoff,et al.  Dust Explosions in the Process Industries , 1991 .

[7]  Rolf K. Eckhoff,et al.  Current status and expected future trends in dust explosion research , 2005 .

[8]  Laurent Perrin,et al.  Explosions of vapour/dust hybrid mixtures: A particular class , 2009 .

[9]  Ernesto Salzano,et al.  Dust/gas mixtures explosion regimes , 2011 .

[10]  Michael J. Pegg,et al.  The ignitability of coal dust-air and methane-coal dust-air mixtures , 1993 .

[11]  V. D. Sarli,et al.  CFD simulations of turbulent fluid flow and dust dispersion in the 20 liter explosion vessel , 2013 .

[12]  Chad V. Mashuga,et al.  The effect of particle size polydispersity on the explosibility characteristics of aluminum dust , 2014 .

[13]  A. D. Benedetto,et al.  Study of the severity of hybrid mixture explosions and comparison to pure dust–air and vapour–air explosions , 2011 .

[14]  K. Cashdollar Coal dust explosibility , 1996 .

[15]  de Lph Philip Goey,et al.  On the determination of the laminar burning velocity from closed vessel gas explosions , 2003 .

[16]  M. G. Zabetakis Flammability characteristics of combustible gases and vapors , 1964 .

[17]  M. Hertzberg,et al.  20‐l explosibility test chamber for dusts and gases , 1985 .

[18]  Richard A. Thomas,et al.  Flammability of methane, propane, and hydrogen gases , 2000 .

[19]  Chad V. Mashuga Determination of the combustion behavior for pure components and mixtures using a 20-liter sphere , 1999 .

[20]  E. Ramalho,et al.  Explosibility of cork dust in methane/air mixtures , 2006 .

[21]  Rolf K. Eckhoff,et al.  Review of the explosibility of nontraditional dusts , 2012 .

[22]  Kenneth L. Cashdollar,et al.  Laboratory and Mine Dust Explosion Research at the Bureau of Mines , 1987 .

[23]  Wolfgang Bartknecht,et al.  Explosions, course, prevention, protection , 1981 .