107 - 107 |
Teaching process safety Louvar JF |
108 - 108 |
Why Hazard evaluation and inherently safer reviews are important to chemical engineering undergraduates Murphy JF |
108 - 108 |
Untitled Theis AE |
109 - 109 |
Responding to december 2012 editorial urgent message to universities Vaughen BK |
110 - 110 |
Untitled Burka M |
113 - 118 |
The safety and chemical engineering education committeebroadening the reach of chemical engineering process safety education Spicer TO, Willey RJ, Crowl DA, Smades W |
119 - 121 |
Keep a sense of vulnerability: For safety's sake Sanders RE |
122 - 125 |
Supporting materials for teaching process safety Louvar JF |
126 - 130 |
Process safety educational determinants Amyotte PR |
131 - 135 |
Risk assessment of a propane storage sphere: Maintain or decommission? Carpenter AR, Ogle RA, Ramirez JC |
136 - 139 |
A simple and cost effective method for determination of the self-accelerating decomposition temperature Fauske HK |
140 - 141 |
Management of changeenabler or inhibitor? Kelly BD |
142 - 145 |
Inherently safer design concepts applied to laboratories Theis AE, Askonas CF |
146 - 151 |
Process safety leadership: Becoming street smart on process safety Wurst D, Cornelisen J |
152 - 159 |
One company's near miss programsuccesses, learning, and improvements Kadri S, Peters G, VanOmmeren J |
160 - 164 |
Linking LOPA and value engineering Norton KD, Surmeli S, Maher ST |
165 - 169 |
On the validation of safeguards for process hazards analysis Baybutt P |
170 - 174 |
Investigating process safety near misses to improve performance Nesmith G, Keating JT, Zacharias LA |
175 - 178 |
Quality problems as process safety warning signs Herber JW |
179 - 184 |
The importance of leadership and management in process safety King C |
185 - 188 |
Correlating process safety leading indicators with performance Forest JJ, Kessler K |
189 - 192 |
Explosibility of a urea dust sample Thomas JK, Kirby DC, Going JE |
193 - 198 |
An experimental investigation of evaporation rates for different volatile organic compounds Heymes F, Aprin L, Bony A, Forestier S, Cirocchi S, Dusserre G |
199 - 206 |
Propagation of a vapor cloud detonation from a congested area into an uncongested area: Demonstration test and impact on blast load prediction Thomas JK, Goodrich ML, Duran RJ |
207 - 211 |
Challenges with the use of CFD for major accident dispersion modeling Plasmans J, Donnat L, de Carvalho E, Debelle T, Marechal B, Baillou F |
212 - 216 |
Modeling of underground hydrogen pipelines Lutostansky E, Creitz L, Jung S, Schork J, Worthington D, Xu YF |
217 - 221 |
Human error analysis of the Macondo well blowout Smith P, Kincannon H, Lehnert R, Wang QS, Larranaga MD |
222 - 223 |
Herrig brothers propane tank explosion [Anonymous] |
226 - 228 |
Safety & Health News Murphy JF |