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Chemicals and Petrochemicals

Chemicals and Petrochemicals Getting Started Resources

Model Predictive Control

Economic MPC Control of Ethylene Oxide Production - Example
Nonlinear MPC Control of an Ethulene Oxidation Plan - Example
Design a Model Predictive Controller for a CSTR in Simulink - Example
Design a Model Predictive Controller by Linearizing a Nonlinear Plant in Simulink - Example

Adaptive MPC Control of a Nonlinear Chemical Reactor:

Using Online Model Estimation - Example
Using Successive Linearization - Example
Using Linear Parameter Varying System - Example

System Identification

PID Controller Tuning for a Model with Discontinuities

Design a PID controller for a model that cannot be linearized. Use system identification to identify a plant model from simulation input-output data.

Fault Detection Using Data Based Models - Example
Fault Detection Using an Extended Kalman Filter - Example
Condition Monitoring and Prognostics Using Vibration Signals - Example
System Identification | Data-Driven Control (4:12) - Video
Estimating Transfer Function Models for a Heat Exchanger - Example
Nonlinear State Estimation Using an Unscented Kalman Filter - Example
Fault Detection and Diagnosis in Chemical and Petrochemical Processes (3 videos) - Video Series

Process Control

Decoupling Controller for a Distillation Column

Decoupling Controller for a Distillation Column

Decouple the two main feedback loops in a distillation column.

Process Control with Reinforcement Learning (15:34) - Video
Simulink CSTR Simulation and Control - File Exchange
Gain-Scheduled Control of a Chemical Reactor - Example
Optimize Multi-Loop Controller Parameters of a Distillation Column Producing Methanol - Example
Independently Control Feedback Loops in a Distillation Column - Example
Temperature Control in a Heat Exchanger - Example
Distillation Controller Tuning - Example

Other Resources

Linearization of a Pulp Paper Process

Linearization of a Pulp Paper Process

Linearize a pulp and paper process model at steady state operating point.

Optimize the Dimensions of a CSTR to Minimize Cost and Variation in Concentration with Changing Feed Stock - Example
Chemical Kinetics with MATLAB - File Exchange
Regression Strategies for Large Datasets - Article
MATLAB for Chemical Reaction Engineering - Community
Cybersecurity of Chemical Plants - Community
Optimizing Scheduling and Blending Operations in the Process Industries (32:00) - Video

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