263 - 263 |
Definition of inherent safety Moore D |
264 - 264 |
Definition of inherent safety Dowell AM |
265 - 265 |
Chemical plants - Inherent safety Hendershot D |
266 - 266 |
Pharma and semiconductor - Inherent safety Moore B |
266 - 266 |
Dust hazards - Inherent Safety Murphy JF |
267 - 267 |
In summary - Inherent safety Rosen B |
268 - 273 |
History of the Loss Prevention Symposia: Forty years, 1967-2006 Davenport JA |
274 - 279 |
A real-life example of choosing an inherently safer process option Study K |
280 - 289 |
Containment system design Leung J, Greenfield W |
290 - 297 |
Relief system's last line of defense, only line of defense.? Melhem GA |
298 - 302 |
Explosible dusts, US codes and standards of safe management practices Kaelin DE, Prugh RW |
303 - 310 |
Characterization and safe handling of reactive initiator solutions Klein JA, Mros GR |
311 - 316 |
Flare case histories demonstrating problems and solutions Straitz JF |
317 - 325 |
Practical designs for inerting in production plants Hoppe T, Jaeger N |
326 - 330 |
Some safety aspects on the design of sparger systems for the oxidation of organic liquids Weber M |
331 - 338 |
Random, systematic, and common cause failure: How do you manage them? Gentile M, Summers AE |
339 - 344 |
Plant safety and risk with temporary equipment Cadwallader LC |
345 - 349 |
CSB investigation of the explosions and fire at the BP Texas City refinery on March 23, 2005 Holmstrom D, Altamirano F, Banks J, Joseph G, Kaszniak M, Mackenzie C, Shroff R, Cohen H, Wallace S |