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III.
Additional PID Design and Tuning Concepts
Exploring Deeper: Sample Time,
Parameter Scheduling, Plant-Wide Control
Sample Time is a Fundamental Design and Tuning Specification
Parameter Scheduling and Adaptive Control of Nonlinear Processes
Plant-Wide Control Requires a Strong PID Foundation
Tuning Using Closed-Loop (Automatic
Mode) Data
Ziegler-Nichols Closed-Loop Method a Poor Choice for Production Processes
Controller Tuning Using Set Point Driven Data
Do Not Model Disturbance Driven Data for Controller Tuning
Evaluating Controller Performance
Comparing Controller Performance Using Plot Data
Cascade Control For Improved Disturbance Rejection
The Cascade Control Architecture
An Implementation Recipe for Cascade Control
A Cascade Control Architecture for the Jacketed Stirred Reactor
Cascade Disturbance Rejection in the Jacketed Stirred Reactor
Feed Forward with Feedback Trim For
Improved Disturbance Rejection
The Feed Forward Controller

Ratio, Override and Cross-Limiting Control (with Allen Houtz)
The Ratio Control Architecture
Ratio Control and Metered-Air Combustion Processes
Override (Select) Elements and Their Use in Ratio Control

Ratio with Cross-Limiting Override Control of a Combustion Process

Integrating (Non-Self Regulating) Processes
(with Bob Rice)
Recognizing Integrating (Non-Self Regulating) Process Behavior
A Design and Tuning Recipe for Integrating Processes
Analyzing Pumped Tank Dynamics with a FOPDT Integrating Model
PI Control of the Integrating Pumped Tank Process
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