Savings Through Fine-Tuning of Process Control Loops
I am working on a project and need your expert guidance and support for some questions related to process control loop optimization. Kindly give point-wise reply to my questions:
1) Is there any savings potential we can talk about if we fine-tune our process control loops (e.g.) fuel flow control loop for boiler or incinerator.
2) What are those applications in which savings can be thought of if fine-tuning is carried out on their associated control loops.
3) Procedure of calculating savings after fine-tuning of specific control loop?
Any support related to my questions is highly appreciated. Thanks.