Chemical Engineering - Plantwide Control of Chemical Processes (English)

   Monday, April 14, 2025   

Starting a new Lecture Notes Series on Chemical Engineering - Plantwide Control of Chemical Processes

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Chemical Engineering - Plantwide Control of Chemical Processes By Lecture Notes together!

Lecture 1: Mod-01 Lec-01 Introduction to the course

Lecture 2: Mod-01 Lec-02 Process Dynamics and Negative Feedback

Lecture 3: Mod-01 Lec-03 PID control

Lecture 4: Mod-01 Lec-04 Common Industrial Control Loops and advanced loops

Lecture 5: Mod-01 Lec-05 Advanced loops (contd) and multivariable systems

Lecture 6: Mod-01 Lec-06 Systematic Tuning Using Frequency Domain Analysis

Lecture 7: Mod-01 Lec-07 Frequency Domain Analysis

Lecture 8: Mod-01 Lec-08 Multivariable Systems

Lecture 9: Mod-01 Lec-09 RGA and dynamic decoupling

Lecture 10: Mod-01 Lec-10 Model based control

Lecture 11: Mod-01 Lec-11 Dynamic Matrix Control

Lecture 12: Mod-01 Lec-12 Control of Distillation Columns

Lecture 13: Mod-01 Lec-13 Temperature inferential distillation control

Lecture 14: Mod-01 Lec-14 Considerations in temperature inferential control

Lecture 15: Mod-01 Lec-15 Control of Complex Column Configurations

Lecture 16: Mod-01 Lec-16 Control of Heat Integrated Columns

Lecture 17: Mod-01 Lec-17 Homogenous extractive distillation

Lecture 18: Mod-01 Lec-18 More on complex columns and reactive distillation

Lecture 19: Mod-01 Lec-19 Control of reactors

Lecture 20: Mod-01 Lec-20 PFR controls (continued) & CSTRs

Lecture 21: Mod-01 Lec-21 CSTR heat management

Lecture 22: Mod-01 Lec-22 Heat Exchangers and Miscellaneous Systems

Lecture 23: Mod-01 Lec-23 Degrees of freedom analysis

Lecture 24: Mod-01 Lec-24 Degrees of freedom (contd)

Lecture 25: Mod-01 Lec-25 Illustration of considerations in control structure synthesis

Lecture 26: Mod-01 Lec-26 Two column recycle process

Lecture 27: Mod-01 Lec-27 Throughput manipulator selection

Lecture 28: Mod-01 Lec-28 Plantwide control structure design

Lecture 29: Mod-01 Lec-29 Systematizing plantwide control design

Lecture 30: Mod-01 Lec-30 The Luyben design procedure

Lecture 31: Mod-01 Lec-31 Role of equipment capacity constraints

Lecture 32: Mod-01 Lec-32 Recycle process case study

Lecture 33: Mod-01 Lec-33 Recycle process case study (contd)

Lecture 34: Mod-01 Lec-34 C4 isomerization process case study

Lecture 35: Mod-01 Lec-35 C4 isomerization process case study (contd)

Lecture 36: Mod-01 Lec-36 C4 isomerization process case study

Lecture 37: Mod-01 Lec-39 C4 isomerization process revisited

Lecture 38: Mod-01 Lec-40 Contrasting conventional and top-down approach

Lecture 39: Mod-01 Lec-41 Cumene process plantwide control

Lecture 40: Mod-01 Lec-37 Systematic economic plantwide control design procedure

Lecture 41: Mod-01 Lec-38 Ethyl benzene process case study