687 - 687 |
Special Issue - Papers Presented at the 2009 International Symposium of the Mary Kay O'Connor Process Safety Center Foreword Mannan MS |
688 - 696 |
ExSys-LOPA for the chemical process industry Markowski AS, Mannan MS |
697 - 704 |
Safety challenges in view of the upcoming hydrogen economy: An overview Pasman HJ, Rogers WJ |
705 - 718 |
Scenario identification and evaluation for layers of protection analysis First K |
719 - 726 |
A toxicity risk assessment method for spill incidents involving volatile liquid hydrocarbons and aqueous solutions in enclosed areas Kazantzis N, Kazantzi V |
727 - 733 |
Beyond-compliance uses of HAZOP/LOPA studies Johnson RW |
734 - 739 |
Azodicarboxylates: Explosive properties and DSC measurements Berger A, Wehrstedt KD |
740 - 744 |
Evaluative comparison of two methods for SADT determination (UN H.1 and H.4) Malow M, Michael-Schulz H, Wehrstedt KD |
745 - 752 |
Performance metrics for evaluating liquefied natural gas, vapor dispersion models Licari FA |
753 - 761 |
Underwater LNG release: Does a pool form on the water surface? What are the characteristics of the vapor released? Raj PK, Bowdoin LA |
762 - 767 |
LNG trench dispersion modeling using computational fluid dynamics Melton TA, Cornwell JB |
768 - 772 |
Forced dispersion of LNG vapor with water curtain Rana MA, Mannan MS |
773 - 780 |
Computational fluid dynamics simulation of fog clouds due to ambient air vaporizers Gavelli F |
781 - 783 |
Overfill protective systems - Complex problem, simple solution Summers AE, Hearn W |
784 - 795 |
Integrating switchgear breakers and contactors into a safety instrumented function Grattan D, Nicholson S |
796 - 798 |
Maintaining the corporate memory Chosnek J |
799 - 805 |
Why bad things happen to good people Mostia WL |
806 - 812 |
Leading and lagging: Process safety climate-incident relationships at one year Payne SC, Bergman ME, Rodriguez JM, Beus JM, Henning JB |
813 - 823 |
Risk assessment and land-use planning regulations in France following the AZF disaster Taveau J |
824 - 830 |
A new approach for facility siting using mapping risks on a plant grid area and optimization Jung S, Ng D, Laird CD, Mannan MS |
831 - 842 |
Sub-cooled and flashing liquid jets and droplet dispersion I. Overview and model implementation/validation Witlox HWM, Harper M, Oke A, Bowen PJ, Kay P |
843 - 848 |
Advanced CFD modeling on vapor dispersion and vapor cloud explosion Qiao A, Zhang S |
849 - 856 |
Sub-cooled and flashing liquid jets and droplet dispersion II. Scaled experiments and derivation of droplet size correlations Kay PJ, Bowen PJ, Witlox HWM |
857 - 877 |
Validation of FLACS against experimental data sets from the model evaluation database for LNG vapor dispersion Hansen OR, Gavelli F, Ichard M, Davis SG |
878 - 884 |
A study on the effect of trees on gas explosions Bakke JR, van Wingerden K, Hoorelbeke P, Brewerton B |
885 - 906 |
Using computational fluid dynamics (CFD) for blast wave predictions Hansen OR, Hinze P, Engel D, Davis S |
907 - 912 |
Dust explosion hazard assessment Ebadat V |
913 - 920 |
The UK Buncefield incident - The view from a UK risk assessment engineer Herbert I |
921 - 927 |
The potential for vapour cloud explosions - Lessons from the Buncefield accident Johnson DM |
928 - 935 |
Common operations failure modes in the process industries Bullemer P, Laberge JC |
936 - 953 |
20 Years on lessons learned from Piper Alpha. The evolution of concurrent and inherently safe design Singh B, Jukes P, Poblete B, Wittkower B |
954 - 957 |
An obituary: ICI's contribution to process safety and why it came to an end Kletz TA |