| 1 |
A simple and cost effective method for determination of the self-accelerating decomposition temperature
Fauske HK
Process Safety Progress, 32(2), 136, 2013 |
| 2 |
Total flammable mass and volume within a vapor cloud produced. by a continuous fuel-gas or volatile liquid-fuel release
Epstein M, Fauske HK
Journal of Hazardous Materials, 147(3), 1037, 2007 |
| 3 |
Managing chemical reactivity - Minimum best practice
Fauske HK
Process Safety Progress, 25(2), 120, 2006 |
| 4 |
Revisiting DIERS' two-phase methodology for reactive systems twenty years later
Fauske HK
Process Safety Progress, 25(3), 180, 2006 |
| 5 |
A fast thermal activity interpreter for controlling chemical reaction hazards
Fauske HK
Process Safety Progress, 23(2), 108, 2004 |
| 6 |
A practical approach to capacity certification - By using certified single-phase flow information in an asymptotic equation form, plants can certify the capacity of pressure-relief valves in two-phase flow
Fauske HK
Chemical Processing, 66(2), 47, 2003 |
| 7 |
Flammable mass and length of a variable-density buoyant fuel jet: Gaussian versus top-hat profiles
Epstein M, Fauske HK
Combustion Science and Technology, 175(7), 1333, 2003 |
| 8 |
Expanded-metal networks: A safety net to thwart gas explosions (vol 97, pg 66, 2001)
Fauske HK, Henry RE
Chemical Engineering Progress, 98(1), 10, 2002 |
| 9 |
Expanded-metal networks: A safety net to thwart gas explosions
Fauske HK, Henry RE
Chemical Engineering Progress, 97(12), 66, 2001 |
| 10 |
Applications of the turbulent entrainment assumption to immiscible gas-liquid and liquid-liquid systems
Epstein M, Fauske HK
Chemical Engineering Research & Design, 79(4), 453, 2001 |
