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FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 1 of 6
Department of Chemical Engineering
LP: CH6602
Rev. No: 00
Date: 05/1/2017B.E/B.Tech/M.E/M.Tech : B.Tech Regulation:2013
PG Specialisation : NA
Sub. Code / Sub. Name : CH6602/ Chemical Reaction Engineering I
Unit : I
Unit Syllabus: Rate equation, elementary, non-elementary reactions, theories of reaction rate and
Prediction; Design equation for constant and variable volume batch reactors, analysis of experimental
kinetics data, integral and differential analysis.
Objective: To impart knowledge on the concepts of reaction kinetics and the interpretation of kinetic data.
Session
No *
Topics to be covered Ref
Teaching
Aids
1
Introduction to Reaction Kinetics, Rate equation with
examples
T1 – Ch 1; pg. 1-8
T2 – Ch 1; pg. 1-7
PPT
2 Elementary & non-elementary reactions T1 – Ch 2; pg. 13-21 PPT
3 Theories of reaction rates T1 – Ch 2; pg.27-29 BB, PPT
4 Temperature dependence of reaction rates
T3 – Ch 3; pg.91-98
T1 – Ch 3; pg.72-74
BB, PPT
5
Analysis of experimental reaction data & their interpretation in
deriving at the rate constants for various order of the reactions
T3 – Ch 13; pg. 868 BB, PPT
6
Integral method of analysis of data for constant and variable
volume reactors, problems
T1 – Ch 3; pg. 41-63 BB, PPT
7
Differential method of analysis of data for constant and
variable volume reactors
T1 – Ch 3; pg.63-67 BB, PPT
8 Design equation of constant volume batch reactor
T1 – Ch 3; pg. 38-41
T1 – Ch 5; pg. 90-94 BB, PPT
9 Design equation of variable volume batch reactor T1 – Ch 3; pg. 67-71 BB, PPT
Content beyond syllabus covered (if any): Deriving the mechanism for a enzyme catalyzed reaction: Michaelis -Menten
Equation
* Session duration: 50 minutes
FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 2 of 6
Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I
Unit : II
Unit Syllabus: Design of continuous reactors - stirred tank and tubular flow reactor, recycle reactors,
combination of reactors, size comparison of reactors.
Objective: To understand the design concepts of ideal reactors and impart the knowledge regarding the
combination of reactor systems.
Session
No *
Topics to be covered Ref
Teaching
Aids
10 Design equations for continuous reactors - CSTR T1 – Ch 5; pg. 94-96 BB, PPT
11
Problems – Using design equations to find volume,
conversion in CSTR
T1 – Ch 5; pg. 96-100 BB, PPT
12 Design equations for PFR T1 – Ch 5; pg. 101-104 BB, PPT
13
Problems – Using design equations to find volume,
conversion in PFR
T1 – Ch 5; pg. 104-110 BB, PPT
14 Performance equation of recycle reactors T1 – Ch 6; pg. 136 -138 BB, PPT
15
Problems – Using performance equation of recycle
reactors
T1 – Ch 6; pg. 139 -140 BB, PPT
16
Multiple reactor systems – Arrangement of reactors in
series/parallel
T1 – Ch 6; pg.124-130 BB, PPT
17 Problems – multiple reactor systems T1 – Ch 6; pg.125,129,130 BB, PPT
18 Size comparison of reactors T1 – Ch 6; pg.120 - 124 BB, PPT
Content beyond syllabus covered (if any): Design equation for semi-batch reactors
* Session duration: 50 mins
FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 3 of 6
Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I
Unit: III
Unit Syllabus: Design of reactors for multiple reactions - consecutive, parallel and mixed reactions -
factors affecting choice, optimum yield and conversion, selectivity, reactivity and yield.
Objective: To learn the underlying concepts of maximizing yield and selectivity
Session
No *
Topics to be covered Ref
Teaching
Aids
19
Multiple reactions – Consecutive, parallel and mixed
reactions
T1 – Ch 8; pg. 170 -176 BB, PPT
20 Design of reactors for multiple reactions T1 – Ch 8; pg. 170 -176 BB, PPT
21
Factors affecting the choice of reactors for single and
multiple reactors.
T1 – Ch 8; pg. 176 -200 BB, PPT
22 Optimum yield & conversion T1 – Ch 7; pg. 152- 161 BB, PPT
23 Selectivity for consecutive, parallel reactions T1 – Ch 7; pg. 158 BB, PPT
24 Selectivity and yield for mixed reactions T1 – Ch 7; pg. 158 BB, PPT
25
Maximization of yield and selectivity for the desired
reaction in different reactor schemes
T1 – Ch 8; pg. 176-181 BB, PPT
26 Problems – Finding optimum yield and conversion T1 – Ch 7; pg. 159- 164 BB, PPT
27 Problems – Finding optimum yield and conversion T1 – Ch 7; pg. 159- 164 BB, PPT
Content beyond syllabus covered (if any): Interpretation of batch reactor data for auto-Catalytic reactions
FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 4 of 6
Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I
Unit: IV
Unit Syllabus: Non-isothermal homogeneous reactor systems, adiabatic reactors, rates of heat exchanges
for different reactors, design for constant rate input and constant heat transfer co-efficient, operation of
batch and continuous reactors, optimum temperature progression.
Objective: To learn the concepts of isothermal and non-isothermal operation of chemical reactors.
Session
No *
Topics to be covered Ref
Teaching
Aids
28 Non-isothermal homogeneous reactor systems T1 – Ch 9; pg. 207 - 210 BB, PPT
29 Adiabatic reactors T3 – Ch 8; pg. 486 - 489 BB, PPT
30 Rate of Heat exchanges for different reactors T3 – Ch 8; pg. 495-497 BB, PPT
31
Design for constant rate heat input and constant heat
transfer coefficient
T3 – Ch 9; pg. 504-511 BB, PPT
32
Batch and Continuous reactors, Equilibrium
conversions at different temperatures
T3 – Ch 8; pg. 511 – 515
T1 – Ch 9; pg. 211 - 215
BB, PPT
33
Optimum temperature progression in CSTR & PFR
Systems
T1 – Ch 13; pg. 868 BB, PPT
34 Heat effects- Adiabatic Operations T1 – Ch 9; pg. 220-223 BB, PPT
35 Heat effects- Non-adiabatic Operations T1 – Ch 9; pg. 220-225 BB, PPT
36 Optimum temperature progression, Reaction Stability T1 – Ch 9; pg. 219-220 BB, PPT
Content beyond syllabus covered (if any): Effect of temperature on product distribution in multiple reactions
FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 5 of 6
Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I
Unit: V
Unit Syllabus: The residence time distribution as a factor of performance; residence time functions and
relationship between them in reactor; basic models for non-ideal flow; conversion in non-ideal
reactors
Objective: To understand the non-ideality in chemical reactors.
Session
No *
Topics to be covered Ref
Teaching
Aids
37 Introduction to Non-Ideal Reactors
T3 – Ch 13; pg. 868
T1 – Ch 11; pg. 257-259
BB, PPT
38
Residence Time Distribution Studies, Stimulus Response
Techniques, Pulse and Step Input, Other Types of Inputs
T3 – Ch 13; pg. 871 – 876
T1 – Ch 11; pg. 261-263
BB, PPT
39
Definition of C, E and F Curves and Relationship between
these Curves.
T3 – Ch 13; pg. 878
T1 – Ch 11; pg. 260-266
BB, PPT
40
Problems illustrating the mean residence time, E (t) curve.
Micro and macro mixing with examples
T3 – Ch 13; pg. 881 – 884
T1 – Ch 11; pg. 267-269
BB, PPT
41 Reactor Modeling using RTD Data, Zero Parameter model T3 – Ch 13; pg. 902 - 904 BB, PPT
42
One Parameter model - Tanks-in series model, Determining
E (θ) & standard mean deviation
T3 – Ch 14; pg. 947
T1 – Ch 14; pg. 321-334
BB, PPT
43 Variance, problems related to finding the number of tanks.
T3 – Ch 14; pg. 948
T1 – Ch 14; pg. 321-334
BB, PPT
44
Dispersion model, open-open boundary conditions,
Definition of Vessel Dispersion Number and Peclet Number
T3 – Ch 14; pg. 955-970
T1 – Ch 13; pg. 293-316
BB, PPT
45 Problems T1,T3 BB, PPT
Content beyond syllabus covered (if any): Derivation of Dispersion model – closed and open vessel, Dispersion model
with reaction
FT/GN/68/01/23.01.16
SRI VENKATESWARA COLLEGE OF ENGINEERING
COURSE DELIVERY PLAN - THEORY
Page 6 of 6
TEXT BOOKS:
1. Levenspiel O, “Chemical Reaction Engineering”, Wiley Eastern Ltd., II Edition, 2000.
2. Smith, J.M, “Chemical Engineering Kinetics”, McGraw Hill, III Edition, 1981.
3. Fogler.H.S., “Elements of Chemical Reaction Engineering”, Prentice Hall of India Ltd., IIIrd
Edition, 2000.
REFERENCE:
1. Froment. G.F. & K.B.Bischoff, “Chemical Reactor Analysis and Design”, John Wiley and Sons,
1979
Prepared by Approved by
Signature
1.
2.
Name
1. Prof. C. Anand Babu
2. G. Saraswathi Dr. N. Meyyappan
Designation
1. Professor
2. Asst. Professor Professor and Head
Date
Remarks *: Nil
Remarks *: Nil
* If the same lesson plan is followed in the subsequent semester/year it should be mentioned
and signed by the Faculty and the HOD

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Ch6602(1)

  • 1. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 1 of 6 Department of Chemical Engineering LP: CH6602 Rev. No: 00 Date: 05/1/2017B.E/B.Tech/M.E/M.Tech : B.Tech Regulation:2013 PG Specialisation : NA Sub. Code / Sub. Name : CH6602/ Chemical Reaction Engineering I Unit : I Unit Syllabus: Rate equation, elementary, non-elementary reactions, theories of reaction rate and Prediction; Design equation for constant and variable volume batch reactors, analysis of experimental kinetics data, integral and differential analysis. Objective: To impart knowledge on the concepts of reaction kinetics and the interpretation of kinetic data. Session No * Topics to be covered Ref Teaching Aids 1 Introduction to Reaction Kinetics, Rate equation with examples T1 – Ch 1; pg. 1-8 T2 – Ch 1; pg. 1-7 PPT 2 Elementary & non-elementary reactions T1 – Ch 2; pg. 13-21 PPT 3 Theories of reaction rates T1 – Ch 2; pg.27-29 BB, PPT 4 Temperature dependence of reaction rates T3 – Ch 3; pg.91-98 T1 – Ch 3; pg.72-74 BB, PPT 5 Analysis of experimental reaction data & their interpretation in deriving at the rate constants for various order of the reactions T3 – Ch 13; pg. 868 BB, PPT 6 Integral method of analysis of data for constant and variable volume reactors, problems T1 – Ch 3; pg. 41-63 BB, PPT 7 Differential method of analysis of data for constant and variable volume reactors T1 – Ch 3; pg.63-67 BB, PPT 8 Design equation of constant volume batch reactor T1 – Ch 3; pg. 38-41 T1 – Ch 5; pg. 90-94 BB, PPT 9 Design equation of variable volume batch reactor T1 – Ch 3; pg. 67-71 BB, PPT Content beyond syllabus covered (if any): Deriving the mechanism for a enzyme catalyzed reaction: Michaelis -Menten Equation * Session duration: 50 minutes
  • 2. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 2 of 6 Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I Unit : II Unit Syllabus: Design of continuous reactors - stirred tank and tubular flow reactor, recycle reactors, combination of reactors, size comparison of reactors. Objective: To understand the design concepts of ideal reactors and impart the knowledge regarding the combination of reactor systems. Session No * Topics to be covered Ref Teaching Aids 10 Design equations for continuous reactors - CSTR T1 – Ch 5; pg. 94-96 BB, PPT 11 Problems – Using design equations to find volume, conversion in CSTR T1 – Ch 5; pg. 96-100 BB, PPT 12 Design equations for PFR T1 – Ch 5; pg. 101-104 BB, PPT 13 Problems – Using design equations to find volume, conversion in PFR T1 – Ch 5; pg. 104-110 BB, PPT 14 Performance equation of recycle reactors T1 – Ch 6; pg. 136 -138 BB, PPT 15 Problems – Using performance equation of recycle reactors T1 – Ch 6; pg. 139 -140 BB, PPT 16 Multiple reactor systems – Arrangement of reactors in series/parallel T1 – Ch 6; pg.124-130 BB, PPT 17 Problems – multiple reactor systems T1 – Ch 6; pg.125,129,130 BB, PPT 18 Size comparison of reactors T1 – Ch 6; pg.120 - 124 BB, PPT Content beyond syllabus covered (if any): Design equation for semi-batch reactors * Session duration: 50 mins
  • 3. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 3 of 6 Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I Unit: III Unit Syllabus: Design of reactors for multiple reactions - consecutive, parallel and mixed reactions - factors affecting choice, optimum yield and conversion, selectivity, reactivity and yield. Objective: To learn the underlying concepts of maximizing yield and selectivity Session No * Topics to be covered Ref Teaching Aids 19 Multiple reactions – Consecutive, parallel and mixed reactions T1 – Ch 8; pg. 170 -176 BB, PPT 20 Design of reactors for multiple reactions T1 – Ch 8; pg. 170 -176 BB, PPT 21 Factors affecting the choice of reactors for single and multiple reactors. T1 – Ch 8; pg. 176 -200 BB, PPT 22 Optimum yield & conversion T1 – Ch 7; pg. 152- 161 BB, PPT 23 Selectivity for consecutive, parallel reactions T1 – Ch 7; pg. 158 BB, PPT 24 Selectivity and yield for mixed reactions T1 – Ch 7; pg. 158 BB, PPT 25 Maximization of yield and selectivity for the desired reaction in different reactor schemes T1 – Ch 8; pg. 176-181 BB, PPT 26 Problems – Finding optimum yield and conversion T1 – Ch 7; pg. 159- 164 BB, PPT 27 Problems – Finding optimum yield and conversion T1 – Ch 7; pg. 159- 164 BB, PPT Content beyond syllabus covered (if any): Interpretation of batch reactor data for auto-Catalytic reactions
  • 4. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 4 of 6 Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I Unit: IV Unit Syllabus: Non-isothermal homogeneous reactor systems, adiabatic reactors, rates of heat exchanges for different reactors, design for constant rate input and constant heat transfer co-efficient, operation of batch and continuous reactors, optimum temperature progression. Objective: To learn the concepts of isothermal and non-isothermal operation of chemical reactors. Session No * Topics to be covered Ref Teaching Aids 28 Non-isothermal homogeneous reactor systems T1 – Ch 9; pg. 207 - 210 BB, PPT 29 Adiabatic reactors T3 – Ch 8; pg. 486 - 489 BB, PPT 30 Rate of Heat exchanges for different reactors T3 – Ch 8; pg. 495-497 BB, PPT 31 Design for constant rate heat input and constant heat transfer coefficient T3 – Ch 9; pg. 504-511 BB, PPT 32 Batch and Continuous reactors, Equilibrium conversions at different temperatures T3 – Ch 8; pg. 511 – 515 T1 – Ch 9; pg. 211 - 215 BB, PPT 33 Optimum temperature progression in CSTR & PFR Systems T1 – Ch 13; pg. 868 BB, PPT 34 Heat effects- Adiabatic Operations T1 – Ch 9; pg. 220-223 BB, PPT 35 Heat effects- Non-adiabatic Operations T1 – Ch 9; pg. 220-225 BB, PPT 36 Optimum temperature progression, Reaction Stability T1 – Ch 9; pg. 219-220 BB, PPT Content beyond syllabus covered (if any): Effect of temperature on product distribution in multiple reactions
  • 5. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 5 of 6 Sub. Code / Sub. Name: CH 6602/ Chemical Reaction Engineering I Unit: V Unit Syllabus: The residence time distribution as a factor of performance; residence time functions and relationship between them in reactor; basic models for non-ideal flow; conversion in non-ideal reactors Objective: To understand the non-ideality in chemical reactors. Session No * Topics to be covered Ref Teaching Aids 37 Introduction to Non-Ideal Reactors T3 – Ch 13; pg. 868 T1 – Ch 11; pg. 257-259 BB, PPT 38 Residence Time Distribution Studies, Stimulus Response Techniques, Pulse and Step Input, Other Types of Inputs T3 – Ch 13; pg. 871 – 876 T1 – Ch 11; pg. 261-263 BB, PPT 39 Definition of C, E and F Curves and Relationship between these Curves. T3 – Ch 13; pg. 878 T1 – Ch 11; pg. 260-266 BB, PPT 40 Problems illustrating the mean residence time, E (t) curve. Micro and macro mixing with examples T3 – Ch 13; pg. 881 – 884 T1 – Ch 11; pg. 267-269 BB, PPT 41 Reactor Modeling using RTD Data, Zero Parameter model T3 – Ch 13; pg. 902 - 904 BB, PPT 42 One Parameter model - Tanks-in series model, Determining E (θ) & standard mean deviation T3 – Ch 14; pg. 947 T1 – Ch 14; pg. 321-334 BB, PPT 43 Variance, problems related to finding the number of tanks. T3 – Ch 14; pg. 948 T1 – Ch 14; pg. 321-334 BB, PPT 44 Dispersion model, open-open boundary conditions, Definition of Vessel Dispersion Number and Peclet Number T3 – Ch 14; pg. 955-970 T1 – Ch 13; pg. 293-316 BB, PPT 45 Problems T1,T3 BB, PPT Content beyond syllabus covered (if any): Derivation of Dispersion model – closed and open vessel, Dispersion model with reaction
  • 6. FT/GN/68/01/23.01.16 SRI VENKATESWARA COLLEGE OF ENGINEERING COURSE DELIVERY PLAN - THEORY Page 6 of 6 TEXT BOOKS: 1. Levenspiel O, “Chemical Reaction Engineering”, Wiley Eastern Ltd., II Edition, 2000. 2. Smith, J.M, “Chemical Engineering Kinetics”, McGraw Hill, III Edition, 1981. 3. Fogler.H.S., “Elements of Chemical Reaction Engineering”, Prentice Hall of India Ltd., IIIrd Edition, 2000. REFERENCE: 1. Froment. G.F. & K.B.Bischoff, “Chemical Reactor Analysis and Design”, John Wiley and Sons, 1979 Prepared by Approved by Signature 1. 2. Name 1. Prof. C. Anand Babu 2. G. Saraswathi Dr. N. Meyyappan Designation 1. Professor 2. Asst. Professor Professor and Head Date Remarks *: Nil Remarks *: Nil * If the same lesson plan is followed in the subsequent semester/year it should be mentioned and signed by the Faculty and the HOD