87 - 87 |
Theodore A (Ted) Ventrone 1916-2008 Davenport JA |
89 - 99 |
Hazard ratings for organic peroxides Duh YS, Wu XH, Kao CS |
100 - 104 |
The mechanical integrity journey-equipment identification Ali SH, Christman R, Frederick JD, Stankovich RJ |
105 - 111 |
Mechanical integrity - Stationary equipment reliability Pinto FW |
112 - 114 |
Taming mechanical integrity Hobbs D |
115 - 120 |
Advances in inherent safety guidance Moore DA, Hazzan M, Rose M, Heller D, Hendershot DC, Dowell AM |
121 - 130 |
Applying the'Limitation of Effects' inherently safer processing strategy when siting and designing facilities Clark DG |
131 - 138 |
Effective training programs using instructional systems design and e-learning Myers PM, Watson B, Watson M |
139 - 144 |
Analysis of management actions, human behavior, and process reliability in chemical plants. II. Near-miss management system selection Meel A, Seider WD, Oktem U |
145 - 152 |
Safety culture factors, group differences, and risk perception in five petrochemical plants Kao CS, Lai WH, Chuang TF, Lee JC |
153 - 155 |
Development of a process safety culture of chemical engineers Mckay M, Lacoursiere JP |
156 - 163 |
The relationship between flash point and LFL with application to hybrid mixtures Prugh RW |
164 - 172 |
The design of duct venting of gas explosions Di Benedetto A, Russo P, Salzano E |
173 - 175 |
Why use CFD for explosion studies? Herrmann DD |