(57b) Non-Traditional Model Predictive Control and Nonlinear Process Modeling for Return on Investment APC Projects
AIChE Spring Meeting and Global Congress on Process Safety
2016
2016 AIChE Spring Meeting and 12th Global Congress on Process Safety
16th Topical Conference on Gas Utilization
Process Simulation, Optimization and Control in Gas Applications II
Monday, April 11, 2016 - 4:00pm to 4:30pm
For example gas processing plants in the field which face huge condensate feed surges known as pigging come from varying conditions in the gas reservoir or the gas and condensate collection system. In addition, there a major production lines that are not continuous but have start/stop operations for clean-in-place and to respond to feed availability changes. These production plants have to have well designed MPC improve process predictability and stability during these transitions.
Handling major process changes or transitions become critical to maximize the return on investment of the advanced control strategy. Success then becomes a sifnficant differentiator from traditional continuous control strategies. This paper addresses new advances in gas processing controls of fractionation, cryogenic processes and even production lines that periodically start and stop and highlights the challenges and methods in the industrial process control practice.