715 - 715 |
Special Issue Papers Presented at the 2010 International Symposium of the Mary Kay O'Connor Process Safety Center Foreword Mannan MS |
716 - 721 |
Safety leadership and safety performance in petrochemical industries: The mediating role of safety climate Wu TC, Chang SH, Shu CM, Chen CT, Wang CP |
722 - 735 |
Compression system check-valve failure hazards Thompson C, King R |
736 - 752 |
Risk-based siting considerations for LNG terminals - Comparative perspectives of United States & Europe Licari FA, Weimer CD |
753 - 757 |
Prediction models for the flash point of pure components Valenzuela EM, Vazquez-Roman R, Patel S, Mannan MS |
758 - 766 |
Class-2 hazmat transportation consequence assessment on surrounding population Chakrabarti UK, Parikh JK |
767 - 773 |
Risk informed optimization of a hazardous material multi-periodic transportation model Kazantzi V, Kazantzis N, Gerogiannis VC |
774 - 779 |
The effects of chemical protective suits on human performance Murray SL, Simon YL, Sheng H |
780 - 790 |
Application of fuzzy logic to explosion risk assessment Markowski AS, Mannan MS, Kotynia A, Pawlak H |
791 - 797 |
The effect of turbulence on the rate of evaporation of LNG on water Morse TL, Kytomaa HK |
798 - 804 |
Medium scale LNG-related experiments and CFD simulation of water curtain Olewski T, Nayak S, Basha O, Waldram S, Vechot L |
805 - 813 |
Anisotropic behavior of energetic materials at elevated pressure and temperature Mota OUO, Cagin T |
814 - 818 |
Common procedural execution failure modes during abnormal situations Bullemer PT, Kiff L, Tharanathan A |
819 - 826 |
Migrating an incident reporting system to a CCPS process safety metrics model Morrison D, Fecke M, Martens J |
827 - 836 |
Highlights of LNG risk technology Pitblado RM, Woodward JL |
837 - 846 |
Does your facility have a dust problem: Methods for evaluating dust explosion hazards Davis SG, Hinze PC, Hansen OR, van Wingerden K |
847 - 851 |
Improving situational awareness through the design of offshore installations Woodcock B, Toy K |
852 - 869 |
Process safety aspects in water-gas-shift (WGS) membrane reactors used for pure hydrogen production Koc R, Kazantzis NK, Ma YH |
870 - 878 |
Modeling the vapor source term associated with the spill of LNG into a sump or impoundment area Ponchaut NF, Kytomaa HK, Morrison DR, Chernovsky MK |
879 - 885 |
Improving PHA/LOPA by consistent consequence severity estimation Summers A, Vogtmann W, Smolen S |
886 - 899 |
Evaporating liquid flow in a channel (An integral model based on shallow water flow approximation) Raj PK |
900 - 907 |
Comparison of calculated data for the flammability and the oxidation potential according to ISO 10156 with experimentally determined values Molnarne M, Schroder V |
908 - 915 |
Evaluating the potential for overpressures from the ignition of an LNG vapor cloud during offloading Gavelli F, Davis SG, Hansen OR |