Understanding dust explosions. The role of powder science and technology

被引:158
作者
Eckhoff, R. K. [1 ,2 ]
机构
[1] Univ Bergen, Dept Phys & Technol, N-5007 Bergen, Norway
[2] Oresund Safety Advisers AB, Malmo, Sweden
关键词
Dust explosions; Dust cloud generation; Ignition; Flame; Propagation; Explosion mitigation; Inherent safety; Powder technology;
D O I
10.1016/j.jlp.2008.07.006
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Dust explosions in the process industries practically always start inside process equipment such as mills, dryers, mixers, classifiers, conveyors, and storage silos and hoppers. For any given dust type the ease with which dust clouds ignite and the rates with which they burn, vary considerably with factors well known in powder science and technology. The key factors include the primary particle size distribution of the dust, the degree of de-agglomeration of the dust particles in the cloud, the dust concentration distribution in the cloud, and the cloud turbulence. The last three factors are entirely dependent on the actual process situation in which the dust cloud is generated and sustained. The paper first discusses influences of these factors on the ignition sensitivity and explosion violence of dust clouds. Secondly, the concept of inherently safer process design to prevent accidental dust explosions is discussed, using design of hoppers and silos as an example. Then some consequences of the mentioned factors in design of mitigatory measures such as explosion isolation, explosion venting, and automatic explosion suppression, are discussed. The role of powder science and technology in understanding development and propagation of secondary dust explosions is also considered. (c) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:105 / 116
页数:12
相关论文
共 21 条
[1]
An inherent safety framework for dust explosion prevention and mitigation [J].
Amyotte, PR ;
Khan, FI .
JOURNAL DE PHYSIQUE IV, 2002, 12 (PR7) :189-196
[2]
[Anonymous], ASTM STP
[3]
[Anonymous], 1845, Philos. Mag., V26, P16
[4]
SIZING OF DUST EXPLOSION VENTS IN THE PROCESS INDUSTRIES - ADVANCES MADE DURING THE 1980S [J].
ECKHOFF, RK .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 1990, 3 (03) :268-275
[5]
ECKHOFF RK, 1977, STAUB REINHALT LUFT, V37, P110
[6]
VENTING OF TURBULENT GAS-EXPLOSIONS IN A 50-M3 CHAMBER [J].
ECKHOFF, RK ;
FUHRE, K ;
GUIRAO, CM ;
LEE, JHS .
FIRE SAFETY JOURNAL, 1984, 7 (02) :191-197
[7]
FISCHER K, 1957, Z ELEKTROCHEM, V61, P685
[8]
THEORETICAL CONSIDERATIONS REGARDING THE INFLUENCES OF PARTICLE-SIZE ON THE MINIMUM IGNITION ENERGY OF DUSTS [J].
KALKERT, N ;
SCHECKER, HG .
CHEMIE INGENIEUR TECHNIK, 1979, 51 (12) :1248-1249
[9]
Review of the DESC project [J].
Skjold, Trygve .
JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES, 2007, 20 (4-6) :291-302
[10]
VIOLENCE OF DUST EXPLOSIONS IN INTEGRATED SYSTEMS [J].
VANWINGERDEN, K ;
PEDERSEN, GH ;
ECKHOFF, RK .
PROCESS SAFETY PROGRESS, 1995, 14 (02) :131-138