11 - 12 |
Why tune control loops? Why make control loops? Latour PR |
15 - 15 |
Reality'bites' for the energy industry Romanow S |
17 - 18 |
Effects of particulate contamination on bearing life Bloch HP |
21 - 21 |
Why do gasoline prices go up and down? Crowley B |
23 - 24 |
In-plant automation support strategies are changing Hill D |
35 - 35 |
Optimal crude oil scheduling software application Kane L, Romanow S |
35 - 36 |
Generation of process pumps designed for peak performance Kane L, Romanow S |
36 - 36 |
Novel incipient surge monitor optimizes compressor operations Kane L, Romanow S |
41 - 41 |
Piping design - Reply Gay JL |
41 - 41 |
Piping design Nesbitt B |
43 - 48 |
Consider process control a specialty within chemical engineering - Part 1 Smith CL |
49 - 50 |
Setpoint tuning method gives excellent response to load changes Robbins LA |
51 - 51 |
Revamping an old pneumatic instrumentation system Vaish VS, Bansal BK |
59 - 64 |
Rationalizing PID tuning with a model-based approach Jaguste DN, Agnihotri RB |
67 - 70 |
Consider a neuro-fuzzy system to model a delayed coking process Jia L, Yu J |
71 - 76 |
Optimize FCC flue-gas emission control - Part 1 Niccum PK, Gbordzoe E, Lang S |
77 - 79 |
Condition monitoring for reciprocating compressors Drewes E |
81 - 84 |
Prevent adsorber bed failure Rahman S |
85 - 88 |
Joint ventures: managing proposals for collaborative successes Lenehan B |
101 - 101 |
Why CFSE certification? Goble W |
103 - 103 |
Monitor microbiological populations in cooling water Huchler LA |