Mod-01 Lec-03 PID control

Course Lectures

• Mod-01 Lec-01 Introduction to the course

  Dr. Nitin Kaistha

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• Mod-01 Lec-02 Process Dynamics and Negative Feedback

  Dr. Nitin Kaistha

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• Mod-01 Lec-03 PID control

  Dr. Nitin Kaistha

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• Mod-01 Lec-04 Common Industrial Control Loops and advanced loops

  Dr. Nitin Kaistha

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• Mod-01 Lec-05 Advanced loops (contd) and multivariable systems

  Dr. Nitin Kaistha

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• Mod-01 Lec-06 Systematic Tuning Using Frequency Domain Analysis

  Dr. Nitin Kaistha

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• Mod-01 Lec-07 Frequency Domain Analysis

  Dr. Nitin Kaistha

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• Mod-01 Lec-08 Multivariable Systems

  Dr. Nitin Kaistha

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• Mod-01 Lec-09 RGA and dynamic decoupling

  Dr. Nitin Kaistha

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• Mod-01 Lec-10 Model based control

  Dr. Nitin Kaistha

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• Mod-01 Lec-11 Dynamic Matrix Control

  Dr. Nitin Kaistha

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• Mod-01 Lec-12 Control of Distillation Columns

  Dr. Nitin Kaistha

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• Mod-01 Lec-13 Temperature inferential distillation control

  Dr. Nitin Kaistha

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• Mod-01 Lec-14 Considerations in temperature inferential control

  Dr. Nitin Kaistha

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• Mod-01 Lec-15 Control of Complex Column Configurations

  Dr. Nitin Kaistha

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• Mod-01 Lec-16 Control of Heat Integrated Columns

  Dr. Nitin Kaistha

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• Mod-01 Lec-17 Homogenous extractive distillation

  Dr. Nitin Kaistha

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

  Dr. Nitin Kaistha

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• Mod-01 Lec-19 Control of reactors

  Dr. Nitin Kaistha

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

  Dr. Nitin Kaistha

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• Mod-01 Lec-21 CSTR heat management

  Dr. Nitin Kaistha

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• Mod-01 Lec-22 Heat Exchangers and Miscellaneous Systems

  Dr. Nitin Kaistha

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• Mod-01 Lec-23 Degrees of freedom analysis

  Dr. Nitin Kaistha

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• Mod-01 Lec-24 Degrees of freedom (contd)

  Dr. Nitin Kaistha

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

  Dr. Nitin Kaistha

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• Mod-01 Lec-26 Two column recycle process

  Dr. Nitin Kaistha

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• Mod-01 Lec-27 Throughput manipulator selection

  Dr. Nitin Kaistha

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• Mod-01 Lec-28 Plantwide control structure design

  Dr. Nitin Kaistha

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• Mod-01 Lec-29 Systematizing plantwide control design

  Dr. Nitin Kaistha

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• Mod-01 Lec-30 The Luyben design procedure

  Dr. Nitin Kaistha

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• Mod-01 Lec-31 Role of equipment capacity constraints

  Dr. Nitin Kaistha

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• Mod-01 Lec-32 Recycle process case study

  Dr. Nitin Kaistha

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

  Dr. Nitin Kaistha

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• Mod-01 Lec-34 C4 isomerization process case study

  Dr. Nitin Kaistha

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

  Dr. Nitin Kaistha

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• Mod-01 Lec-36 C4 isomerization process case study

  Dr. Nitin Kaistha

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• Mod-01 Lec-37 Systematic economic plantwide control design procedure

  Dr. Nitin Kaistha

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• Mod-01 Lec-38 Ethyl benzene process case study

  Dr. Nitin Kaistha

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• Mod-01 Lec-39 C4 isomerization process revisited

  Dr. Nitin Kaistha

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• Mod-01 Lec-40 Contrasting conventional and top-down approach

  Dr. Nitin Kaistha

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• Mod-01 Lec-41 Cumene process plantwide control

  Dr. Nitin Kaistha

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