Home - News ( United States | United Kingdom | Italy | Germany ) - Football scores

Showing content from http://www.controlguru.com/pages/table.html below:

Table of Contents – Control Guru

1) Fundamental Principles of Process Control

• Motivation and Terminology of Automatic Process Control
• The Components of a Control Loop
• Process Data, Dynamic Modeling and a Recipe for Profitable Control
• Sample Time Impacts Controller Performance

2) Graphical Modeling of Process Dynamics: Heat Exchanger Case Study

• Step Test Data From the Heat Exchanger Process
• Process Gain is the “How Far” Variable
• Process Time Constant is the “How Fast” Variable
• Dead Time is the “How Much Delay” Variable
• Validating Our Heat Exchanger Process FOPDT Model

3) Modeling Process Dynamics: Gravity Drained Tanks Case Study

• The Gravity Drained Tanks Process
• Dynamic “Bump” Testing of the Gravity Drained Tanks Process
• Graphical Modeling of Gravity Drained Tanks Step Test
• Modeling Gravity Drained Tanks Data Using Software

4) Software Modeling of Process Dynamics: Jacketed Stirred Reactor Case Study

• Design Level of Operation for the Jacketed Stirred Reactor Process
• Modeling the Dynamics of the Jacketed Stirred Reactor with Software
• Exploring the FOPDT Model With a Parameter Sensitivity Study

5) Process Control Preliminarie

• Design and Tuning Recipe Must Consider Nonlinear Process Behavior
• A Controller’s “Process” Goes From Wire Out to Wire In
• The Normal or Standard PID Algorithm

 6) Proportional Control – The Simplest PID Controller

• The P-Only Control Algorithm
• P-Only Control of the Heat Exchanger Shows Offset
• P-Only Disturbance Rejection of the Gravity Drained Tanks

 7) Caution: Pay Attention to Units and Scaling

• Controller Gain is Dimensionless in Commercial Systems

 8) Integral Action and PI Control

• Integral Action and PI Control
• PI Control of the Heat Exchanger
• PI Disturbance Rejection of the Gravity Drained Tanks
• The Challenge of Interacting Tuning Parameters
• PI Disturbance Rejection in the Jacketed Stirred Reactor
• Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form

 9) Derivative Action and PID Control

• PID Control and Derivative on Measurement
• The Chaos of Commercial PID Control
• PID Control of the Heat Exchanger
• Measurement Noise Degrades Derivative Action
• PID Disturbance Rejection of the Gravity Drained Tanks

10) Signal Filters and the PID with Controller Output Filter Algorithm

• Using Signal Filters In Our PID Loop
• PID with Controller Output (CO) Filter
• PID with CO Filter Control of the Heat Exchanger
• PID with CO Filter Disturbance Rejection in the Jacketed Stirred Reactor

11) 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

12) Controller 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 Use Disturbance Driven Data for Controller Tuning 

13) Evaluating Controller Performance

• Comparing Controller Performance Using Response Plot Data

14) Integrating (Non-Self Regulating) Processes

• 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

15) 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

16) Feed Forward with Feedback Trim For Improved Disturbance Rejection

• The Feed Forward Controller
• Feed Forward Uses Models Within the Controller Architecture  
• Static Feed Forward and Disturbance Rejection in the Jacketed Reactor

17) Ratio, Override and Cross-Limiting Control

• 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

18) Cascade, Feed Forward and Three-Element Control

• Cascade, Feed Forward and Steam Boiler Level Control
• Dynamic Shrink/Swell and Steam Boiler Level Control

19) Distillation Column Control (by Jim Riggs)

• Introduction to Distillation Column Control
• Major Disturbances & First-Level Distillation Column Control
• Inferential Temperature & Single-Ended Column Control
• Dual Composition Control & Constraint Distillation Column Control

20) Discrete Time Modeling of Dynamic Systems (by Peter Nachtwey)

• A Discrete Time Linear Model of the Heat Exchanger

21) Fuzzy Logic and Process Control (by Fred Thomassom)

• Envelope Optimization and Control Using Fuzzy Logic

RetroSearch is an open source project built by @garambo | Open a GitHub Issue

Search and Browse the WWW like it's 1997 | Search results from DuckDuckGo

HTML: 3.2 | Encoding: UTF-8 | Version: 0.7.4