学 术 报 告-Flame Propagation in Hybrid Methane - Coal Dust – Air Flames

发布时间:2014-12-08浏览次数:27

Flame Propagation in Hybrid Methane - Coal Dust – Air  Flames
20141216日(周二)10:00,矿业科学中心A200
Ali S. Rangwala
Associate Professor
Department of Fire Protection Engineering,
Worcester Polytechnic Institute, Worcester, MA 01609 USA
rangwala@wpi.edu
Dust deflagrations or flame propagation in a mixture of flammable particles  (~10 - 100 µm) and air or gases has gained increasing importance in industrial  fire and explosion safety. Every year dust deflagrations in coal mines and  chemical plants cause extensive material damage, injury, and loss of life.  Current guidance for prevention and suppression originates from experiments  performed in simple vessel arrangements, and the parameters used to assess the  hazard of flammable dusts are empirically driven. The problem is thus unresolved  from a fire and explosion safety perspective. From a scientific viewpoint  enhancing our fundamental knowledge of particle combustion lies at the heart of  national security priorities such as energy efficiency and pollution control by  improving the design of power plants. There has also been a recent push towards  studying influence of nano-particulate matter in combustion systems.
In this talk, I will describe the results of laboratory experiments to  identify the controlling parameters of laminar and turbulent hybrid dust  deflagration mechanisms (Xie et al., Comb. Flame, 159, 2449-2456, 2012,  and Rockwell and Rangwala, Comb. Flame, 160, 635-640, 2013). A novel  premixed-dust-air burner is designed to measure the burning velocity of a hybrid  mixture of Pittsburgh seam coal dust, with typical particle sizes in the range  of 25 to 106 µm and methane-air. Figure 1 depicts shadowgraph images of a sample  of flames tested. The results show that adding coal dust in methane-air premixed  flame reduces the burning velocity for laminar flames and  increases as turbulent intensities are increased. Two competing effects  are considered to explain these trends. The first effect is due to volatile  release, which increases the overall equivalence ratio and thus, the burning  velocity. The second is the heat sink effect the coal particles take up to  release the volatiles. A mathematical model is developed considering these  effects. The implications of the work towards numerical modeling of turbulent  particle air flames is discussed
Figure 1: Shadowgraph images of: (a) laminar methane-air flame  (b) laminar methane-air-dust flame (c) turbulent methane-air flame, (d)  turbulent methane-air-dust flame. Methane-air equivalence ratio, Φ = 0.9 for all  cases. Coal-dust particle size = 75 – 90 µm in (b) and (d), and concentration =  70 g/m3. Turbulent intensity u’ = 0.7 m/s for (c) and (d).
演讲人简介
Ali S. Rangwala is an associate professor in the department of Fire  Protection Engineering at Worcester Polytechnic Institute (WPI). He has a BS in  Electrical Engineering, from the Government College of Engineering, Pune,  India (2000), an MS in Fire Protection Engineering from the  University of Maryland, College Park (2002), and a PhD in Mechanical and  Aerospace Engineering from the University of California, San Diego (2006).  Professor Rangwala’s research interests are in the area of industrial fire and  explosions. His recent projects include, deflagration of combustible dust  clouds, ignition behavior of combustible dust layers, in-situ burning of oil,  spread of an oil slick in channels, velocity measuring techniques in fire  induced flows, and flame propagation and burning rate behavior of condensed fuel  surfaces.