Blogs

How can we provide Mechanical and Process Engineering Regulatory Control Guidance Tips (Part 2)?

In part 2 we evaluate a misleading statement about the amount of derivative to use and provide some better guidance. We take a look at how mechanical and process design and operating conditions affect the need for derivative action.

How can we provide Mechanical and Process Engineering Regulatory Control Guidance Tips (Part 1)?

The mechanical, piping, and process design determines the steady state and integrating process gains and the process deadtimes and lags. The process engineer usually sets the project basis for the control system in the development of the Process Flow Diagram (PFD) and in the writing of the operating and process descriptions.

What Are the Merits of Options to avoid a Kick on a Setpoint Change Tips?

The PID structures with proportional on error cause a step change in the PID output for a large setpoint change. For structures with derivative on error there is also a sharp bump almost looking like a spike unless you zoom in.

Is it better to have a Controller with More or Less Knobs Tips?

What are the relative merits of different PID structures, a setpoint (SP) filter, and analog output (AO) setpoint rate (velocity) limits? Should I seek a general solution I can use all the time and each knob fits a particular purpose, or a controller with fewer knobs that does exactly what...

How do you Effectively Use Anti-Reset Windup Options Tips?

Anti-reset windup (ARW) protection is a standard feature of industrial PID controllers. In some DCS, ARW limits are adjustable besides output limits.  The ARW limits may not be at their best values. ARW default values may not match up with output limits as output scale and engineering units change.

The ABCs of Controller Tuning

All of the major tuning methods end up with the same expressions for PID gain, reset time, and rate time when the tuning objective is maximum disturbance rejection. Differences come down to tweaking of the a, b, and c coefficients.

Who Says the single loop controller is dead? Not ABB, that's for sure! #APW2010 #pauto

ABB announces new generation of controller and indicator instruments Elevates process monitoring and control to a higher level