petrotrinsmerv
Chemical
- Apr 16, 2003
- 12
Currently we are preparing to implement a new MPC controller on one of our process plants. Generally, the approach used is where the relationships between manipulated variables (MVs, also called 'handles), controlled variables (CVs, or targets) and disturbance variables (DVs) are defined based on available (or generated data) , identified and modelled, thereby characterising the overall process or unit op as a 'Black Box'. It has been suggested that there is an advantage to a 'Gray Box' approach where the relationships between CVs may also be identified and modelled. However, I haven't heard (yet) what possible advantages may be derived from this. I believe, with my limited experience, that a well built 'Black Box' model, especially used in conjunction with good soft-sensors should be more than sufficient for any but the most difficult of processes. Does anyone have another perspective on this?