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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.
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Webinar Recording: Strange but True Process Control Stories
Listen to Greg McMillan's lessons learned the hard way during a 40-year career in process control industries. Many of the mistakes made in the field are still being made today, some posing safety riskBy: Gregory K. McMillan06 June, 2018 | 1 minutes -
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Webinar Recording: Temperature Measurement and Control
Temperature is the most important common measurement that is critical for process efficiency and capacity.By: Gregory K. McMillan23 April, 2018 | 1 minutes -
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What are New Technologies and Approaches for Batch and Continuous Process Control?
For any type of analysis or prediction, whether using ANN or MSPC, you need to have inputs that show the variability in the process.By: Gregory K. McMillan08 January, 2018 | 11 minutes -
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What Are Best Practices and Standards for Control Narratives?
When creating detailed control narratives for existing controls, use established standards and industry best practices.By: Gregory K. McMillan04 December, 2017 | 4 minutes -
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When and How to Use Derivative Action in a PID Controller
The least frequently used mode in a PID controller, derivative is more useful when dead time is not pure dead time but is a series of small time constants.By: Gregory K. McMillan22 November, 2017 | 6 minutes -
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How to Manage Pipeline Valve Positioner and PID Tuning
In general use the highest valve positioner gain that does not cause oscillation. For pipeline flow and pressure control, oscillations are not filtered.By: Gregory K. McMillan06 November, 2017 | 8 minutes -
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Webinar Recording: How to Get the Most Out of Control Valves
The data that is really needed when selecting and sizing a control valve is rarely understood and specified.By: Gregory K. McMillan19 June, 2017 | 1 minutes -
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How to Overcome Challenges of PID Control and Analyzer Applications via Wireless Measurements
An enhanced PID controller simplifies tuning and improves loop stability and reliability for loops dominated by discontinuous measurement updates.By: Gregory K. McMillan22 May, 2017 | 8 minutes -
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Feedforward Control Enables Flexible, Sustainable Manufacturing
Feedforward provides preemptive corrective action for production rate and grade changes enabling key PID controllers to provide consistent product quality.By: Gregory K. McMillan01 May, 2017 | 13 minutes -
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PID Controller Tuning Rules
Safety, equipment and environmental protection, process efficiency and capacity, product quality, and control system maintenance depend on PID tuning.By: Gregory K. McMillan17 April, 2017 | 9 minutes -
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What Are Best Cutover Strategies for Upgrading an Industrial Plant?
When retrofitting an industrial plant, review budget, schedule, financial justification for the project, as well as all areas of concern such as shutdown.By: Gregory K. McMillan19 December, 2016 | 10 minutes -
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How to Avoid Common Tuning Mistakes With PID Controllers
The success of advanced control depends on the basic control system foundation. The PID controller is the common key component of all control loops.By: Gregory K. McMillan05 October, 2016 | 15 minutes -
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The Good, Bad, and Ugly of Thermal Mass Flowmeters
Thermal mass flowmeters can be a relatively inexpensive flowmeter that can handle extremely small and large flowsBy: Gregory K. McMillan29 August, 2016 | 5 minutes -
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PID Tuning for Near and True Integrating Processes
The most important loops on vessels and columns typically have a near or true integrating response.By: Gregory K. McMillan08 August, 2016 | 8 minutes -
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What are the Equivalent Methods to Eliminate Proportional Step and Derivative Kick?
There are several methods for eliminating or controlling the proportional step and derivative kick in a PID output resulting from a change of setpoint.By: Gregory K. McMillan25 January, 2016 | 5 minutes -
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What Is the Definition of PID Bumpless Transfer?
Bumpless transfer and how a new operating point can be achieved quickly and smoothly after the PID is switched to automatic mode.By: Gregory K. McMillan28 December, 2015 | 6 minutes -
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How Do You Measure Control System Performance?
Seek a suite of practical metrics in terms of key performance indicators that can have an impact on plant control system performance.By: Gregory K. McMillan02 December, 2015 | 4 minutes -
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How Do You Convert Tuning Settings of an Independent PID?
Considerable confusion exists on how the PID Form affects tuning settings. Lack of understanding of Form & units of settings can lead to disastrous results.By: Gregory K. McMillan04 November, 2015 | 7 minutes -
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How to Better Understand Integrating and Runaway Process Dynamics
Technical discussion on how to improve industrial automation operations by understanding integrating and runaway process dynamicsBy: Gregory K. McMillan21 September, 2015 | 4 minutes -
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Better Process Control by Understanding Self-Regulating Process Dynamics
The three types of processes in the automation industry are self-regulating, integrating, and runaway.By: Gregory K. McMillan07 September, 2015 | 6 minutes -
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Benefits of Good Tuning: Increased Production and Profitability, Reduced Variability
For control loop tuning, the first settings that must be right are the controller and valve actions. If these actions are not right, nothing else matters.By: Gregory K. McMillan02 September, 2015 | 6 minutes -
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How to Achieve Tight Process Recirculation Temperature Control
How to eliminate oscillations associated with the discontinuity and changes in phase between heating and cooling and make the response of the secondary temperature loop faster.By: Gregory K. McMillan29 July, 2015 | 5 minutes -
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How to Make Transitions Between Cooling and Heating Smooth and Fast
How eliminate oscillations associated with the discontinuity and changes in phase between heating and cooling and make the response of the secondary temperature loop faster.By: Gregory K. McMillan15 July, 2015 | 6 minutes -
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How to Optimize Cascade Control Systems in Vessel Heating and Cooling
How to make sure the cascade control system is intelligently designed to meet process requirements in terms of vessel and heat transfer surface temperaturesBy: Gregory K. McMillan24 June, 2015 | 7 minutes -
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What are the Critical Aspects of Jacket and Coil Design in Vessel Heating and Cooling?
Critical aspects of the design of the jacket and coil in vessel heating and cooling.By: Gregory K. McMillan17 June, 2015 | 6 minutes -
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Simple Strategies for Maximizing Biopharmaceutical Product Quality
Use of key PID features, tuning objectives and feedforward control can meet the stringent requirements for biopharmaceutical production.By: Gregory K. McMillan27 May, 2015 | 5 minutes -
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Simple Strategies for Optimizing Ethanol Plants
PID controllers for front-end production rate, slurry concentration & average fermentation time can decrease costs and increase production rates for ethanol plants.By: Gregory K. McMillan13 May, 2015 | 7 minutes -
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Optimizing Multiphase Reactors with a Single Phase Product
Multiphase reactors offer an inherent ability to optimize excess reactant concentration by the proper use of a simple pressure or temperature control loop.By: Gregory K. McMillan22 April, 2015 | 4 minutes -
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Getting the Most Out of Fluidized Bed Reactors
The fast kinetics and composition response of a fluidized bed reactor enable the direct manipulation of reactant feed rate by temperature control to inherently maximize production rate to the coolantBy: Gregory K. McMillan13 April, 2015 | 5 minutes -
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Maximizing Production Rate of Single Phase Liquid Reactors
Control schemes for maximizing production rate in liquid reactorsBy: Gregory K. McMillan18 March, 2015 | 5 minutes -
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Achieving Tight Control of Single Phase Liquid Reactors
How to set up control loops for liquid reactors to achieve their full potential.By: Gregory K. McMillan09 March, 2015 | 6 minutes -
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Temperature Sensor Installation for Best Response and Accuracy
Best practices to get the most out of the inherent capability of a temperature sensor.By: Gregory K. McMillan16 February, 2015 | 6 minutes -
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Temperature Communication for Best Accuracy and Reliability, and Least Noise
How the advent of smart transmitters and wireless communication has opened the door to better temperature communication & process performance improvements.By: Gregory K. McMillan04 February, 2015 | 7 minutes -
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What are the Inherent Differences in the Performance of Pure Batch, Fed-Batch and Continuous Reactors?
A look at the differences between pure batch versus fed-batch versus continuous reactors.By: Gregory K. McMillan19 January, 2015 | 5 minutes -
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An Overview of the Control Loops for Batch, Fed-Batch and Continuous Reactors
A look at how many of the loops can be the same and how all reactors benefit from a more extensive application of feedback control.By: Gregory K. McMillan12 January, 2015 | 3 minutes -
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What are the Implications of Industrial Reactor Type on Control?
The effect of reactor type on dynamic response, allowable measurement lags and delays, controller tuning, and control strategies is significant.By: Gregory K. McMillan22 December, 2014 | 8 minutes -
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How to Obtain Concentration Measurements from Common Inline Sensors
To control the concentration of key components, relatively inexpensive inline measurements can be used under the right conditions to provide concentration measurementsBy: Gregory K. McMillan08 December, 2014 | 4 minutes -
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Inferential Measurement of Cell and Crystal Growth Rate and Reaction Rate
Simple online inferential measurements of cell growth rate, crystal growth rate, and chemical reaction rate are possible using conventional online measurements of flow and temperature.By: Gregory K. McMillan24 November, 2014 | 5 minutes -
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Automation Project and Startup Humor – How to Laugh Rather Than Fret
Automation Project and Startup Humor – How to Laugh Rather Than FretBy: Gregory K. McMillan07 November, 2014 | 3 minutes -
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Have You Had a Good Automation Industry Laugh Today?
Humor can provide insights by opening the mind to the strange but true aspects of the industrial automation profession. Successful humor can cause a smile before you realize the full nature of the sitBy: Gregory K. McMillan20 October, 2014 | 2 minutes -
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How to Select the Optimal Temperature Sensor for Industrial Applications
How to Select the Optimal Temperature Sensor for Industrial ApplicationsBy: Gregory K. McMillan08 September, 2014 | 3 minutes -
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Top 10 Mistakes Made Every Day in pH System Design
In pH control systems reagent piping and injection must minimize transportation delays, volumes must have proper geometry and agitation to maximize the process time constant that filters pH oscillatioBy: Gregory K. McMillan18 August, 2014 | 2 minutes -
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What are the Essentials of pH in Industrial Applications?
What are the Essentials of pH in Industrial Applications?By: Gregory K. McMillan06 August, 2014 | 7 minutes -
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Continuous Improvement in an Automation Career Requires Continuous Solicitation of Feedback
An individual should never stop learning and improving. You cannot improve unless you know what you are doing wrong.By: Gregory K. McMillan20 June, 2014 | 4 minutes -
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How to Use Plant-Wide Feedforward for More Flexible and Efficient Production
The use of plant-wide feedforward control can move a plant quickly and smoothly for more flexible and efficient manufacturing.By: Gregory K. McMillan13 June, 2014 | 11 minutes -
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Why You Should Scrutinize Technical Articles for Bias
If an article is written by the sales and marketing department, be on the lookout for a biased view of a product or service.By: Gregory K. McMillan06 June, 2014 | 3 minutes -
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What are the Benefits of Identifying Deadtime and Ramp Rate?
The identification of deadtime and ramp rate can provide tuning, rapid modeling, and future values for smart reset, feedforward, and setpoint responses.By: Gregory K. McMillan30 May, 2014 | 5 minutes -
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High Pay Is Not Reason Enough to Stay in a Bad Industrial Automation Job
When interviewing for a position, interview your perspective boss as hard as he (or she) is interviewing you.By: Gregory K. McMillan23 May, 2014 | 4 minutes -
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How to Smooth the Transition Between Batch and Continuous Operations
The unbalance between continuous operation flow & instantaneous batch flow can be spread over available inventory by an adapted rate limited feedforward.By: Gregory K. McMillan16 May, 2014 | 4 minutes -
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Why References Are Just the First Step in an Industrial Employee or Control Systems Evaluation
Treat references as a first step toward engaging a wider group who can provide a more realistic picture of the person or product or company being evaluated.By: Gregory K. McMillan09 May, 2014 | 5 minutes
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