Learn · Plant Design and Economics
Lecture 34 of 63WEEK 07
Lecture 34: Reactor Synthesis for Complex Reactions by Attainable Region: Example-2
Prof. Debasis Sarkar · IIT Kharagpur
Credits and licence
- From
- Plant Design and Economics, IIT Kharagpur (at NPTEL)
- Licence
- CC BY-NC-SA, as NPTEL states it. Non-commercial use only.
- Attribution
- NPTEL states: "Distributed under Creative Commons Attribution-ShareAlike / CC BY - NC - SA", beside a BY-NC-SA badge.
- Who can watch
- Tweens profiles and older. How courses are placed
All the lectures
- Lecture 01: Introduction
- Lecture 02: Typical Design Steps
- Lecture 03: Flow Diagram
- Lecture 04: Flow Diagram - Mass and Energy Balance
- Lecture 05: Piping and Instrumentation Diagram
- Lecture 06: Selection of Process Equipment
- Lecture 07: Process Utilities
- Lecture 08: Plant Location
- Lecture 09: Site and Plant Layout
- Lecture 10: Heuristics in Process Synthesis and Design
- Lecture 11: Capital Investment
- Lecture 12: Capital Cost Estimates
- Lecture 13: Cost Components in Capital Investments
- Lecture 14: Methods of Capital Cost Estimates
- Lecture 15: Estimation of Total Product Cost
- Lecture 16: Different Types of Interest
- Lecture 17: Continuous Interest, Cash Flow Diagram, Time Value of Money
- Lecture 18: Uniform Cash Flows and Continuous Flows
- Lecture 19: Income Tax and Depreciation
- Lecture 20: Depreciation
- Lecture 21: Cumulative Cash Flow and Profitability Standards
- Lecture 22: Profitability Analysis
- Lecture 23: Profitability Analysis (Contd.)
- Lecture 24: Profitability Analysis (Contd.)
- Lecture 25: Alternative Investment, Replacement and Sensitivity Analysis
- Lecture 26: Introduction to Process Synthesis
- Lecture 27: Hierarchical Approach to Process Synthesis - I
- Lecture 28: Hierarchical Approach to Process Synthesis - II
- Lecture 29: Hierarchical Approach to Process Synthesis - III
- Lecture 30: Hierarchical Approach to Process Synthesis - IV
- Lecture 31: Basic Reactor Principles
- Lecture 32: Reactor Synthesis for Complex Reactions by Attainable Region: Fundamentals
- Lecture 33: Reactor Synthesis for Complex Reactions by Attainable Region: Example-1
- Lecture 34: Reactor Synthesis for Complex Reactions by Attainable Region: Example-2
- Lecture 35: General Procedure for Reactor Design and Cost Estimation
- Lecture 36: Introduction to Separation Systems
- Lecture 37: Selection Criteria for Separation Processes
- Lecture 38: Design of Multi-component Distillation Column: Short Cut Method
- Lecture 39: Design of Multi-component Distillation Column: Short Cut Method - Example
- Lecture 40: Introduction to Sequencing of Ordinary Distillation Columns
- Lecture 41: Sequences for Simple Nonintegrated Distillation Columns
- Lecture 42: Distillation Sequencing using Columns with Sidestreams
- Lecture 43: Distillation Sequencing using Thermal Coupling
- Lecture 44: Azeotropic Distillation: Residue Curve Maps
- Lecture 45: Azeotropic Distillation Methods and Cost Estimation
- Lecture 46: Introduction to Pinch Technology
- Lecture 47: Composite Curves
- Lecture 48: The Problem Table Method
- Lecture 49: The Heat Recovery Pinch and The Grand Composite Curve
- Lecture 50: Heat Exchanger Network Design
- Lecture 51: Introduction
- Lecture 52: Fires and Explosion: Flammability Characteristics
- Lecture 53: Fires and Explosions: Prevention
- Lecture 54: Toxic Release, Hazard Identification and MSDS
- Lecture 55: Inherently Safer Design
- Lecture 56: Optimality Criteria for Unconstrained Functions
- Lecture 57: Examples
- Lecture 58: Equality Constrained Problems: Langrange Multipliers
- Lecture 59: Linear Programming Problems
- Lecture 60: Batch Process Scheduling
- Live Session 19-10-2020
- Live Session 30-11-2020
- Live Session 10-12-2020