1 - 1 |
The 12th international symposium on loss prevention and safety promotion in the process industries translating knowledge into practice Considine M, Suter G |
3 - 13 |
Hazards equal trips or alarms or both Timms C |
14 - 20 |
Dust explosions: How should the influence of humidity be taken into account? Traore M, Dufaud O, Perrin L, Chazelet S, Thomas D |
21 - 25 |
"Total risk of death"-Towards a common and usable basis for consequence assessment Rushton AG, Carter DA |
26 - 34 |
From laboratory simulation to scale-up and design of spray barriers mitigating toxic gaseous releases Palazzi E, Curro F, Fabiano B |
35 - 39 |
Application of inherent safety principles to dust explosion prevention and mitigation Amyotte PR, Pegg MJ, Khan FI |
40 - 46 |
SDG-based HAZOP analysis of operating mistakes for PVC process Wang HZ, Chen BZ, He XR, Tong Q, Zhao JS |
47 - 52 |
Distinction between the upper explosion limit and the lower cool flame limit in determination of flammability limit at elevated conditions Pekalski AA, Pasman HJ |
53 - 58 |
Main differences on European regulations in the frame of the Seveso Directive Pey A, Lerena P, Suter G, Campos J |
59 - 63 |
The major accident risk (MAR) process - developing the profile of major accident risk for a large multi national oil company Considine M, Hall SM |
64 - 69 |
Measurement of charge transfer during filling and emptying FIBC Glor M, Muller P, Kubainsky C |