1 - 3 |
Transitions within the process safety community Crowl D |
4 - 18 |
Enhanced NOAA Chemical Reactivity Worksheet for Determining Chemical Compatibility Gorman D, Farr J, Bellair R, Freeman W, Frurip D, Hielscher A, Johnstone H, Linke M, Murphy P, Sheng M, van Gelder K, Viveros D |
19 - 25 |
Guidelines for Determining the Probability of Ignition of a Released Flammable Mass Stack B, Sepeda A, Moosemiller M |
26 - 35 |
Bow-tie diagrams in downstream hazard identification and risk assessment Saud YE, Israni K, Goddard J |
36 - 40 |
The ALARP Principle in Process Safety Baybutt P |
41 - 48 |
Managing process safety information based on process safety management requirements Aziz HA, Shariff AM, Rusli R |
49 - 55 |
Is the Safe Performance of Flame Gaps in Flameproof Electrical Apparatus Deteriorated by Rusting and Mechanical Damage? Part 2: Group IIB and IIC Gases Arntzen BJ, Ringdal L, Steiner M, Eckhoff RK |
56 - 63 |
Simulation study on an explosion accident in china Zhao XD, Jiang CM, Wang YP, Yuan JW, Wang Z |
64 - 69 |
A mechanistic and experimental study on the diethyl ether oxidation Di Tommaso S, Rotureau P, Sirjean B, Fournet R, Benaissa W, Gruez P, Adamo C |
70 - 76 |
Flammable State and Dilution Requirement in the Theoretical Flammability Diagram Ma TG, Larranaga M |
77 - 84 |
Risk analysis by means of a QRA approach on a LPG cylinder filling installation Dormohammadi A, Zarei E, Delkhosh MB, Gholami A |
85 - 93 |
Hazard effects of high-speed flow from methane-hydrogen premixed explosions Ma QJ, Zhang Q, Pang L |
94 - 103 |
Explosion from a smoldering silo fire Ogle RA, Dillon SE, Fecke M |