235 - 241 |
Calculation of Fire and Explosion Index (F&EI) value for the Dow Guide taking credit for the loss control measures Gupta JP, Khemani G, Marman MS |
243 - 248 |
Ignition of a dust layer by a constant heat flux Lebecki K, Dyduch Z, Fibich A, Sliz J |
249 - 257 |
Thermal explosion of autocatalytic reaction El-Sayed SA |
259 - 269 |
The use of water sprays for mitigating chlorine gaseous releases escaping from a storage shed Dimbour JP, Dandrieux A, Gilbert D, Dusserre G |
271 - 279 |
Development and applications of CASEHAT - a multipurpose computer aided hazard analysis automation system used in semiconductor manufacturing industry I YP |
281 - 288 |
Critical and transition conditions of gaseous explosion El-Sayed SA |
289 - 296 |
The runaway scenario in the assessment of thermal safety: simple experimental access by means of the catalytic decomposition of H2O2 Eissen M, Zogg A, Hungerbuhler K |
297 - 303 |
Fire incident at a refinery in West Malaysia: the causes and lessons learned Shaluf IM, Ahmadun FR, Said AM |
305 - 311 |
Risk assessment of major hazards: the effect of ground slope Hankin RKS |
313 - 321 |
Dynamic management of human error to reduce total risk Jo YD, Park KS |
323 - 331 |
Modeling of detonation processes in chemically active bubble systems at normal and elevated initial pressures Fomin PA, Mitropetros K, Hieronymus H |
333 - 340 |
Simple devices to prevent dust explosion propagation in charge chutes and pipes Holbrow P, Tyldesley A |
341 - 347 |
Evaluation of a CFD porous model for calculating ventilation in explosion hazard assessments Fothergill CE, Chynoweth S, Roberts P, Packwood A |
351 - 351 |
Investigation of the Fushun ASU explosion in 1997 (vol 16, pg 209, 2003) Lehman JY, Wei XC, Hua QX, Delannoy G |