Lecture 1 - Introduction to the course
Lecture 2 - Process Dynamics and Negative Feedback
Lecture 3 - PID control
Lecture 4 - Common Industrial Control Loops and advanced loops
Lecture 5 - Advanced loops (Continued...) and multivariable systems
Lecture 6 - Systematic Tuning Using Frequency Domain Analysis
Lecture 7 - Frequency Domain Analysis
Lecture 8 - Multivariable Systems
Lecture 9 - RGA and dynamic decoupling
Lecture 10 - Model based control
Lecture 11 - Dynamic Matrix Control
Lecture 12 - Control of Distillation Columns
Lecture 13 - Temperature inferential distillation control
Lecture 14 - Considerations in temperature inferential control
Lecture 15 - Control of Complex Column Configurations
Lecture 16 - Control of Heat Integrated Columns
Lecture 17 - Homogenous extractive distillation
Lecture 18 - More on complex columns and reactive distillation
Lecture 19 - Control of reactors
Lecture 20 - PFR controls (Continued..) & CSTRs
Lecture 21 - CSTR heat management
Lecture 22 - Heat Exchangers and Miscellaneous Systems
Lecture 23 - Degrees of freedom analysis
Lecture 24 - Degrees of freedom (Continued...)
Lecture 25 - Illustration of considerations in control structure synthesis
Lecture 26 - Two column recycle process
Lecture 27 - Throughput manipulator selection
Lecture 28 - Plantwide control structure design
Lecture 29 - Systematizing plantwide control design
Lecture 30 - The Luyben design procedure
Lecture 31 - Role of equipment capacity constraints
Lecture 32 - Recycle process case study
Lecture 33 - Recycle process case study (Continued...)
Lecture 34 - C4 isomerization process case study
Lecture 35 - C4 isomerization process case study (Continued...)
Lecture 36 - C4 isomerization process case study
Lecture 37 - Systematic economic plantwide control design procedure
Lecture 38 - Ethyl benzene process case study
Lecture 39 - C4 isomerization process revisited
Lecture 40 - Contrasting conventional and top-down approach
Lecture 41 - Cumene process plantwide control
