Mod-01 Lec-40 Contrasting conventional and top-down approach | Courses.com

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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