Contents of Reaction Engineering - Video Lecture Course

Contents of Reaction Engineering - Video Lecture Course Reaction Engineering - Video Lectures on Short Theory, Problems with Detailed Solutions

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Learn the Essentials in 10 Hours

Class-1
Class-2
Class-3
Class-4

Theory

Quick Review of Theory - Part-1

Quick Review of Theory - Part-2

Kinetics of Homogeneous Reactions

Arrhenius Model of Rate Constant
Molecularity of Reaction
Order of Reaction and Units of Rate Constant
Order of Reaction from Conversion Data
Constant Volume Reactions in Batch Reactor
Conversion of Half-Order Reaction
Rate Expression from Conversion Data
Upper Limit of Reaction Rate
First Order Reversible Reaction
Time Constant of First Order Reversible Reaction
Maximum Conversion of Reversible Reaction
Enzymatic Reaction
First Order Variable Volume Reaction
Rate of Formation or Consumption of Each Components
Rate of Formation / Consumption of Components of Reaction
Extent of Reaction and Conversion
Order of Reaction from Rate vs Concentration
Order of Reaction from Half-life Data
Reaction Order with Half-life Time Equaling Fifty Percent of Full-life Time
Half-life vs Initial Concentration - Straight Line Plot
Inert Content for a Variable Volume Reaction
Decomposition of N2O5 - Non-elementary Reaction
Decomposition of Azomethane - Steps Involved
Mechanism of Non-elementary Reaction

Single Ideal Reactor for Single Reactions

Enzymatic Reaction in Batch Reactor
Gas-phase Reaction in Batch Reactor - Constant Volume / Constant Pressure
Relation for Conversion of Gas-phase Reaction in Batch Reactor
Variable Volume Reaction in Constant Pressure Reactor
Variable Volume Reaction in PFR
Variable Volume Reaction in PFR with Pressure Data
Second-order Liquid-phase Reaction in CSTR
Second Order Variable Volume Reaction in PFR
Kinetics of Second Order Reaction from MFR
Second Order Bi-Molecular Reaction in PFR
Second Order Bimolecular Reaction in MFR
Pressure of Batch Reactor with Gas-phase Reaction
Reversible First Order Reaction in PFR
Reversible First Order Reaction in MFR
Reversible Reaction in MFR
Radioactive Reaction in MFR
Enzymatic Reaction in PFR
Enzymatic Reaction in MFR
Variable Volume First Order Reaction in MFR
Equilibrium Constant of Gaseous / Liquid Phase Reaction
Variable Volume Reaction - Effect of Temperature
Second Order Gas-phase Reaction in Batch Reactor
Mass Balance of Semi-batch Reactor
Conversion of Zero Order Reaction in CSTR
Volume of Reactors from Levenspiel Plot
Plug Flow Reactor with Separation and Recycle

Reactor Combinations for Single Reactions

Second Order Reaction in Two MFRs in Series
Radioactive Reaction in Two MFRs in Series
MFR followed by PFR for Second Order Reaction
PFR Replacing Two MFR in Series
Radioactivity at the End of Two CSTRs in Series
Kinetics from MFRs in Series
Replacing CSTR with Two-Smaller CSTRs
Autocatalytic Reaction in PFR / MFR / Combinations
Recycle Reactor
Replacing MFRs with PFR
First Order Reaction in CSTRs in Series
CSTRs in Series - First Order Reaction
Arrangement of Reactors for Second Order Reaction
Reactors in Series - First Order Reaction
Reactors in Series - Second Order Reaction
Reactor Combinations for Minimum Volume

Multiple Reactions

Mole Balance in Multiple Reactions
Selectivity of Parallel Reactions
Maximizing the Yield with 3 Parallel Reactions
Parallel Reactions in MFR
Parallel Reactions in MFRs in Series - First Order
Parallel Reactions in MFRs in Series
Parallel Reactions in PFR
Parallel Reactions in PFR - Rate Constants for the given Product Distribution
Parallel Reactions in PFR - First and Zeroth Order Reactions
Temperature of PFR for the given Product Distribution
Parallel Reactions in Batch Reactor
Conditions Maximizing a Parallel Reaction in MFR
Parallel Reactions in MFR - Ex-2
Parallel BiMolecular Reactions in CSTR - First and Second Order Reactions
Maximizing the Desired Product - 3 Parallel Reactions in MFR
Series Reactions in PFR and MFR
Series Reactions in PFR and MFR - Example-2
Maximizing the Yield with Series Reactions
Series Reactions in Batch Reactor - First Order followed by Zeroth Order
Reactor for Maximizing the Desired Product from Yield Plot

Temperature Effects

Conversion of Isomer in a Continuous Adiabatic Reactor
Feed Composition for a given Reaction Temperature
Product Flowrate with Endothermic Reaction
Temperature Rise in Adiabatic Reactor
Heat Removed from CSTR
Maximum Allowable Feed Temperature of MFR
Volume of MFR for Reversible Adiabatic Reaction
Exothermic Gas-phase Reaction in Adiabatic CSTR
Exothermic First Order Reaction in CSTR
Reactor Volume and Feed Temperature of CSTR
Adiabatic MFR for First Order Isomerization Reaction
Irreversible Endothermic Reaction in Adiabatic PFR
Temperature Profile for Minimizing Volume of PFR for Reversible Exothermic Reaction
Heat Removal from CSTR - Bi-molecular Second Order Reaction
Conversion vs. Temperature of Exothermic Reaction

Non-ideal Reactors

Residence Time from C-curve - Triangular
Residence Time from C-curve - Rectangular
Mean Residence Time from E-curve
Conversion of Parallel Reactions in Non-ideal Reactor
Conversion of Second Order Reaction in Non-ideal Reactor
Volume Ratio of PFR to MFR from E-curve
Useful Volume of Reactor from E-curve
Identifying Reactors from Pulse Input
RTD of Two Reactors in Series
Identifying Reactors from Step Input
RTD Studies with Step Input
Identifying Reactors from Pulse Input
Conversion from Exit Age Distribution

Langmuir-Hinshelwood-Hougen-Watson Models

Langmuir Isotherm
First Order Reversible Reaction - Surface Reaction Controlling
Second Order Reversible Reaction - Surface Reaction Controlling
Irreversible Bimolecular Reaction - Surface Reaction Controlling
Irreversible Reaction with Non-adsorbing Product - Surface Reaction Controlling
Irreversible Reaction following Rideal Mechanism - Surface Reaction Controlling
Second Order Reversible Reaction - Desorption of Product - Rate Controlling
Molecular and Dissociative Adsorptions
Reaction Consisting of Molecular and Dissociative Adsorption

Heterogeneous Reactions

Effective Rate Constant of Heterogeneous Reaction with Non-porous Catalyst
Conversion of Reaction - with Decaying Catalyst Activity
Activity of Catalyst
Observed Order of Reaction with Porous Catalyst
Activation Energy of Catalytic Reaction
Reaction with Porous Catalyst at Large Thiele Modulus
Effectiveness of Heterogeneous Catalytic Reaction
Role of Pore Diffusion and External Mass Transfer - Example-1
Role of Pore Diffusion and External Mass Transfer - Example-2
First Order Reaction in Packed Bed Reactor in Strong Pore Diffusion Regime
Rate vs. Particle Size of Catalyst - Pore Diffusion Controlling
Rate Controlling Step of Non-Catalytic Reaction - Shrinking Core Model

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