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Gregory K. McMillan
Gregory K. McMillan retired as a Senior Fellow from Solutia Inc in 2002 and as a senior principal software engineer from Emerson Process Systems and Solutions Simulation R&D in 2023. Greg is an ISA Fellow and the author of more than 200 articles and papers, 100 Q&A posts, 80 blogs, 200 columns, and 20 books. He was one of the first inductees into the Control Process Automation Hall of Fame in 2001, and he received the ISA Lifetime Achievement Award in 2010, the ISA Mentor Award in 2020, and the ISA Standards Achievement Award in 2023.
271 Results Found
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Why a Virtual Plant Is Crucial for Process Control Improvement
A virtual plant provides uses the actual plant’s control system & operator interface crucial for training and all levels of process control improvement.By: Gregory K. McMillan28 December, 2012 | 5 minutes -
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The Benefits of Learning the Industrial Codes
Try to learn at least one relevant industrial code or one code section each year and seek to apply that knowledge often so that it is not lost.By: Gregory K. McMillan22 December, 2012 | 4 minutes -
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How to Use High Rangeability Flowmeters and Valves to Increase Plant Turndown
To increase plant turndown, use control valves and flow measurements with the best low flow response and precision.By: Gregory K. McMillan14 December, 2012 | 5 minutes -
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How to Specify a Capillary Seal Assembly
Be extremely careful to select knowledgeable technicians to install capillary seals. Many a pipefitter has pulled them out of the box and bolted them up without the proper gaskets and spacers. If thisBy: Gregory K. McMillan08 December, 2012 | 5 minutes -
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How to Maximize Loop Coordination and Optimization
Employ setpoint filters, velocity limits and external-reset feedback to meet the process control objectives at your plant or facility.By: Gregory K. McMillan30 November, 2012 | 4 minutes -
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How to Achieve Best Disturbance Rejection and Setpoint in Industrial Processes
Use disturbance rejection tuning, external-reset feedback, and a setpoint filter in your PID controller to achieve loop performance objectives.By: Gregory K. McMillan30 November, 2012 | 4 minutes -
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The Good, the Bad, and the Ugly of Magmeters
The Good, the Bad, and the Ugly of MagmetersBy: Gregory K. McMillan23 November, 2012 | 4 minutes -
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How to Eliminate Split Range Oscillations in Process Control
Use precise valves, scheduled tuning, external-reset feedback, directional rate setpoint limits, and an enhanced PID to stop split range oscillations.By: Gregory K. McMillan16 November, 2012 | 4 minutes -
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The Value of Process in Designing or Improving an Industrial Control System
Designing and/or improving a control system is practically impossible if the team does not understand the process.By: Gregory K. McMillan09 November, 2012 | 3 minutes -
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Why You Should Not Use On-Off Valves as Control Valves
On-off valves should not be used as control valves (for throttling) and control valves should not be used as on-off valves (for isolation).By: Gregory K. McMillan03 November, 2012 | 5 minutes
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