1 |
Combustion behaviors and explosibility of suspended metal hydride TiH2 dust Cheng YF, Wu HB, Liu R, Yao YL, Su J, Wang WT, Shu CM International Journal of Hydrogen Energy, 45(21), 12216, 2020 |
2 |
Experimental investigations of the ignition delay time, initial ignition energy and lower explosion limit of zirconium powder clouds in a 20 L cylindrical vessel Song XZ, Su H, Xie LF, Li B, Cao Y, Wang YX Process Safety and Environmental Protection, 134, 429, 2020 |
3 |
Determination of the explosion characteristics of methanol - Air mixture in a constant volume vessel Saeed K Fuel, 210, 729, 2017 |
4 |
원료의약품 분진의 폭발 위험성 평가 이주엽, 이근원, 박상용, 한인수 Korean Chemical Engineering Research, 55(5), 600, 2017 |
5 |
Integration of Fire and Explosion Index in3D Process Plant Design Software Mitkowski PT, Bal SK Chemical Engineering & Technology, 38(7), 1212, 2015 |
6 |
Fatty oil hydrogenation in supercritical solvents: Process design and safety issues Ramirez E, Mayorga MJ, Cuevas D, Recasens F Journal of Supercritical Fluids, 57(2), 143, 2011 |
7 |
Laminar burning velocity and explosion index of LPG-air and propane-air mixtures Huzayyin AS, Moneib HA, Shehatta MS, Attia AMA Fuel, 87(1), 39, 2008 |
8 |
The integration of Dow's fire and explosion index (F&EI) into process design and optimization to achieve inherently safer design Suardin J, Mannan MS, El-Halwagi M Journal of Loss Prevention in The Process Industries, 20(1), 79, 2007 |
9 |
Measuring the violence of dust explosions with the "201 sphere" and with the standard "ISO 1 m(3) vessel" - Systematic comparison and analysis of the discrepancies Proust C, Accorsi A, Dupont L Journal of Loss Prevention in The Process Industries, 20(4-6), 599, 2007 |
10 |
Taking credit for loss control measures in the plant with the likely loss fire and explosion index (LL-F&EI) Jensen N, Jorgensen SB Process Safety and Environmental Protection, 85(B1), 51, 2007 |