| 11 - 12 |
What is optimization for the HPI?
Romanow S |
| 11 - 12 |
Top ten reasons to model for optimization
Broussard MR |
| 15 - 15 |
A day with Google
Kane LA |
| 17 - 18 |
Expander power absorption methods
Bloch HP |
| 21 - 21 |
Environmental Technology Centre
Crowley B |
| 31 - 31 |
Sound waves break up sulfur compounds
[Anonymous] |
| 31 - 32 |
Online tube coating inhibitor system
[Anonymous] |
| 32 - 32 |
Fiber optic tank gauging system
[Anonymous] |
| 33 - 33 |
Analyzer features lowest detection level
[Anonymous] |
| 33 - 34 |
Internet-based software for fluids
[Anonymous] |
| 34 - 34 |
First level/flow switches with intrinsic safety
[Anonymous] |
| 39 - 40 |
Bearing life and contamination
Ward T |
| 39 - 39 |
How to control a deethanizer
Shinskey G |
| 39 - 39 |
Decisions about risk reduction
Latour PR |
| 43 - 49 |
How to efficiently plan a grassroots refinery
Maiti SN, Eberhardt J, Kundu S, Cadenhouse-Beaty PJ, Adams DJ |
| 51 - 51 |
Minimize NOx emissions cost-effectively
McAdams JD, Reed SD, Itse DC |
| 63 - 66 |
Increase VCM output
Lee JK, Kang KH, Song KH |
| 69 - 69 |
Crude distillation unit online optimization
Hou K, Li Y, Shen J, Hu S |
| 77 - 77 |
Determine the optimum crude intake level - a case history
Hartmann JCM |
| 85 - 86 |
Improve tray operations
Sloley AW |
| 89 - 89 |
Control valves for critical applications
Kiesbauer J |
| 101 - 101 |
Case 3: Shaft galling in a bushing
Sofronas T |
| 103 - 108 |
Petrochemical plant costs for the new millennium
Sommerfield JT |
| 133 - 133 |
The trend toward SIL2
Goble WM |
| 135 - 136 |
Why automate chemical feed and control systems?
Huchler LA |
| 100A - 100A |
Predict contaminant concentrations in deaerator-vent emissions
Kunz RG, Baade WF |
