| Chemical process safety: fundamentals with applications DA Crowl, JF Louvar Pearson Education, 2001 | 1923 | 2001 |
| Chemical process safety: fundamentals with applications DA Crowl, JF Louvar Pearson Education, 2001 | 1915 | 2001 |
| Understanding explosions DA Crowl John Wiley & Sons, 2010 | 177 | 2010 |
| Health and environmental risk analysis: fundamentals with applications JF Louvar, BD Louvar Prentice Hall, 1998 | 133 | 1998 |
| Individual risk analysis of high-pressure natural gas pipelines YD Jo, DA Crowl Journal of Loss Prevention in the Process Industries 21 (6), 589-595, 2008 | 110 | 2008 |
| The hazards and risks of hydrogen DA Crowl, YD Jo Journal of Loss Prevention in the Process Industries 20 (2), 158-164, 2007 | 104 | 2007 |
| Derivation of Le Chatelier's mixing rule for flammable limits CV Mashuga, DA Crowl Process safety progress 19 (2), 112-117, 2000 | 95 | 2000 |
| Application of the flammability diagram for evaluation of fire and explosion hazards of flammable vapors CV Mashuga, DA Crowl Process Safety Progress 17 (3), 176-183, 1998 | 85 | 1998 |
| Flammability zone prediction using calculated adiabatic flame temperatures CV Mashuga, DA Crowl Process Safety Progress 18 (3), 127-134, 1999 | 80 | 1999 |
| Layer of protection analysis: simplified process risk assessment Center for Chemical Process Safety (CCPS) Wiley, 2011 | 72 | 2011 |
| Flammability envelopes for methanol, ethanol, acetonitrile and toluene MR Brooks, DA Crowl Journal of loss prevention in the process industries 20 (2), 144-150, 2007 | 52 | 2007 |
| Explosion characteristics of hydrogen‐air mixtures in a spherical vessel YD Jo, DA Crowl Process Safety Progress 29 (3), 216-223, 2010 | 46 | 2010 |
| Human factors methods for improving performance in the process industries D Attwood CCPS, Center for Chemical Process Safety, 2007 | 43 | 2007 |
| Flame growth model for confined gas explosion YD Jo, DA Crowl Process Safety Progress 28 (2), 141-146, 2009 | 26 | 2009 |
| Calculating the energy of explosion using thermodynamic availability DA Crowl Journal of loss prevention in the process industries 5 (2), 109-118, 1992 | 26 | 1992 |
| Estimating sonic gas flow rates in pipelines JM Keith, DA Crowl Journal of loss prevention in the process industries 18 (2), 55-62, 2005 | 24 | 2005 |
| Predicting the maximum gas deflagration pressure over the entire flammable range Y Fan, DA Crowl Journal of Loss Prevention in the Process Industries 13 (3-5), 361-368, 2000 | 23 | 2000 |
| The Bhopal tragedy: its influence on process and community safety as practiced in the United States RJ Willey, DA Crowl, W Lepkowski Journal of loss prevention in the process industries 18 (4-6), 365-374, 2005 | 21 | 2005 |
| Identifying criteria to classify chemical mixtures as “highly hazardous” due to chemical reactivity DA Crowl, TI Elwell Journal of Loss Prevention in the Process Industries 17 (4), 279-289, 2004 | 18 | 2004 |
| Sizing pressure-relief devices DA Crowl, SA Tipler Chemical Engineering Progress 109 (10), 68-76, 2013 | 15 | 2013 |
