Voices: McMillan & Weiner

What Are the Benefits of Advanced Process Control?

How Good Is Good? McMillan and Weiner Talk with Lewis Gordon about APC benefit techniques such as Model Predictive Control

By Greg McMillan, Stan Weiner

Stan: This month, we continue the thread we started last month—sharing the experience gained over the 38-year career of Lewis Gordon, a principal control systems engineer retired from Invensys. Last month, we focused on tuning and loop performance monitoring software. Here, we explore how to approach estimating and proving the benefits from applying advanced process control (APC) techniques such as model predictive control (MPC).

Greg: In previous columns and blogs, I advocated the use of a metric to quantify improvements in process efficiency and capacity, preferably in dollars, immediately before and after basic process control improvements such as better field measurements and valves, control strategies and feed-forward control.

Stan: Considering that an MPC can be switched between automatic and manual to show "APC on" and "APC off" performance on demand, we asked Lew, "How do you quantify the economic benefits of an APC project?"

Lew: The previous column listed the three basic metrics for performance improvement— production rate and value, energy consumption per unit of product and yield per unit of feed. Comparing "before" and "after" values for these metrics is the usual approach. Still, many things can change over the course of a project that will cloud the results. Changes in process equipment and characteristics, product specifications and the costs of energy and/or feed will generate changes in these metrics that are unrelated to the project implementation.

So although it's more difficult, expensive and time-consuming, the only truly fair way is to compare averages for these metrics from APC-on and APC-off periods at the end of a project.

Many random things happen in the plant every day that affect control system performance. So the only accurate way to get a good comparison is to expose the "new" and "old" control systems to these random events across a series of APC-on and APC-off periods. The list of such influences is long. Variations in production rate, raw materials properties, fuel characteristics, operator influences, ambient conditions, product demand and quality specifications, upstream and downstream operations, mechanical factors such as equipment modifications, process factors such as fouling and changes in catalyst activity, and field automation system issues such as plugging, sensor coating and valve wear will make themselves felt.

Also read "Bringing Advanced Process Control Home"

The net effect of truly random influences will present itself as a normal distribution of these metrics, calculated for a series of APC-on and APC-off periods. Where the observed distribution is not normal, in the statistical sense, there are specific reasons that need to be identified. For example, averages and medians may be forced apart by nonlinearities as the operating point moves closer to an optimum, forcing the statistical distribution to be asymmetric. In such a case, the standard deviation on the side closest to the optimum is more important.

The rules of statistical analysis and the characteristics of plant dynamics and disturbances define the random tests needed. All "normal" variations can be captured by random on-off testing, with on and off times, sample interval and transition times all based on the plant and MPC response times and known disturbance periods.

The total on and off test time must be long enough to include all combinations of significant variations. The shortest individual test time should be three times the longest settling time. The longest individual test time should be the longest test time plus the longest disturbance interval. Disturbances at known periods and times can be used to set the on and off test boundary (test start and end times).

Finally, data collected during the transition between systems should not be used for calculating performance metrics, as this data will always bias the results in favor of the poorer performing configuration. The minimum transition time should be greater than the larger of the longest disturbance settling time or the optimizer settling time.

Abnormal operation and day-to-night variations, instrument failures, manual control and the like should be removed from the data prior to statistical analysis.

Greg: Dennis Cima alluded to these requirements for documenting MPC performance in Control Talk, July 2013, "The Route to Model Predictive Control Success." Dennis emphasized the need to screen the data and remove outliers before benefits are reported. What are your guidelines on sampling for the statistical analysis of benefits?

Lew: Data sampling intervals should be less than half the shortest process variable period of oscillation to avoid aliasing. Set the sampling interval to be less than 10% of the dominant time constant, but not so short as to simply be capturing noise.

Stan: How do you use results reporting to inspire people, rather than make them perspire?

Lew: Operations should be credited publicly when things go well, but never criticized publicly when things go wrong. You never want to make people look bad in front of their peers. Unfairly preferential praise and criticism both create resentment. The goal is to create team spirit and a common desire to excel.

Greg: What is needed for an APC project to deliver benefits?

Lew: First, don't be penny-wise and pound-foolish. An advanced control performance improvement project of any significant size needs an APC study to provide a solid basis for project definition and planning, and the economic justification that will command the necessary time and resources. A study provides clarification of objectives, priorities and scope. This leads to selection of the most appropriate technology and more realistic scheduling and staffing plans.

A study also can cut project cost by identifying work already done, defining a shorter schedule, eliminating later scope changes, and promoting more efficient project execution. A process study also promotes customer and supplier familiarity, and develops working relationships early on.

Finally, a study increases the probability of success through a better definition of what data and information needs to be provided by the customer and the details of the work to be done. An extreme example of how this can go wrong was one APC project that was sold without a study. When the APC team showed up to execute the project, the customer simply dumped a foot high stack of old Fortran code listings on the table and said, "This is what we have now. We just need you to optimize and implement what this does into the new DCS." After a long struggle, neither side was satisfied with the result, technically or economically.

On the other hand, a process study also can disqualify projects that don't have sufficient potential economic benefits to proceed, thereby avoiding wasting time and money on both sides. A bad project does no one any good—both sides lose.



Greg: I would think getting everyone involved in the study and the project into the meeting, with some understanding of the implications of statements, would be best.

Maybe there is Greg and Stan anti-matter somewhere in the universe who are salesmen. Any meeting would result in a tremendous release of energy and strange matter. This leads us to the "Top 10 Reasons Why Hopefully There is Only One Stan and Greg in the Universe"

10. Greg and Stan "look-alike" contests are more challenging.
9. Automation "Top 10 Lists" are a specialty rather than a commodity.
8. Cartoonist Ted is not overwhelmed with ideas.
7. Engineers aren't inspired to do stand-up comedy routines during project meetings.
6. Young engineers don't aspire to become just like Greg and Stan.
5. Society doesn't get confused by smiling and laughing engineers.
4. Florida gets time to get ready for another Stan, including evacuation plans.
3. ISA standards committees get time to address Greg and Stan statements.
2. Just two wild and crazy guys were too much for management.
1. Anti-matter Greg and Stan are salesmen.

More from this voice

Title

Is Your Control Valve an Imposter?

Beware the Disguised Positioner

11/06/2012

Bringing Advanced Process Control Home

McMilland and Weiner Talk With Arnold Martin About Model-Predictive Control. Read the Column and Learn About Martin's Accomplishments and Perspective

09/26/2012

Get the Most Out of Your Batch

The Same Techniques Used to Get the Most Ethanol Out of a Scarce Corn Crop Can Help You Optimize Other Batch Processes

09/07/2012

Control Loop Improvement

McMillan and Weiner Talk With Jacques Smuts About Improving Control Loops

08/30/2012

Calibration Trends

McMillan and Weiner Ask Glenn Gardner, Fluke Product Planner, to Help Them Complete Their Perspective on Calibration by Taking a Look at Future Trends

08/13/2012

Smart Calibration

How Can You Make Temperature Calibration Faster?

07/16/2012

The Human Factor

What Are the Biggest Problems That Control Engineers Face When Going into a Plant?

06/18/2012

Control Valve Innovations

McMillan and Weiner Asks Hans Baumann About His Most Notable Innovations in Control Valves.

05/14/2012

New Paradigms for Lab Control Systems

What a Lab Control Systems Can and Should Do for Commercialization of Biopharmaceuticals

03/29/2012

Going with the Flow

McMillan and Weiner Continue Their Interview With Ram Ramachandran. They Discuss What Flow Sensor Works Best in Various Applications

03/08/2012

Radar Love

Control Talk Editors, McMillan and Weiner, Ask Industrial Measurement Device Expert Ram Ramachandran About the Use of Radar on the Plant Floor

01/30/2012

Gas Chromatographs Rule

What Comes First--the Analyzer or the Analyzer Application?

01/10/2012

Process Analyzers. Analyze This!

Fewer Analyzer Specialists Are Left Working at the Plant Floor, Could It Be Because Newer Anaylyzer Systems Come Available as Complete Packages?

12/07/2011

The Operations Key to Better Plant Performance

What Have You Done to Help the Operator Get the Most Out of a Control System?

11/15/2011

Don't Over Look PID in APC

That Old Stalwart PID Can Do a Lot of Heavy Lifting in Your Process Control Efforts

11/09/2011

The Maintenance Key to Improved Performance

Getting the Inside Scoop from a Control Engineer on How to Integrate O&M Knowledge and Relationships to Provide Long-Term Highly Successful Solutions

10/17/2011

The Key to Process Knowledge and Sustainable Manufacturing

What Is the Future of Operator Training Systems, and What Are You Doing to Further Simulation Technologies?

09/12/2011

PID World Tour--The Final Performance

Read the Conclusion of McMillan, Weiner and Congiundi's Tour of PID World

08/15/2011

More Fun with PID Controllers

Exploring Just How Flexible and Powerful the PID Controller Can Be

07/11/2011

More Extraordinary PID Innovations

The Creative Use of PID Controllers for Process Improvement

06/13/2011