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Chapter 1
General Overview
Conceptual Design of a chemical process
Q: What is a conceptual design?
A: Finding best flowsheet:
1- selecting appropriate equipment
2- best configuration of the equipment
3- determining optimum operating conditions
How do we categorize the above decisions?
1 & 2 are discrete while 3 is continuous decision
Design variables
Discrete ( no. & type of reactors,…)
1- variables
Continuous ( temperature, pressure,…)
with local effect (reflux ratio,…)
2- variables
with global effect (reactor conversion,…)
Conceptual design is an MINLP optimization problem
Hierarchical nature of process synthesis
Utility system
HEN
Separation
Reactor
Design steps
Outwards
A Typical Chemical Process
Hydrodealkylation of Toluene to produce Benzene (HDA)
Toluene + H2 Benzene + CH4
2 Benzene Diphenyl + H2
T = 1150 – 1300 °F
P = 500 psia
H2
2
2
2 / Toluene @ reactor inlet
/ Toluene @ reactor inlet
/ Toluene @ reactor inlet
/ Toluene @ reactor inlet ≃
≃
≃
≃ 5/1
5/1
5/1
5/1
Purge
Reactor Flash
Toluene
Col.
Benzene
Col.
Stabilizer
H2 , CH4
H2 , CH4
Benzene
Diphenyl
H2 , CH4
H
H
Toluene
C
Compressor
A typical flowsheet
How can we create this flowsheet ?
Let’s simplify the flowsheet first:
1- remove all heat exchangers, drums and storage
vessels
2- group all distillation columns
3- Simplify general structure of separation system
4- Lump complete separation system
5- Lump complete process
Purge
Reactor Flash
Toluene
Col.
Benzene
Col.
Stabilizer
Toluene
H2 , CH4
H2 , CH4
Benzene
Diphenyl
H2 , CH4
Toluene
Purge
Reactor Flash
Toluene
H2 , CH4
H2 , CH4
Benzene
Diphenyl
H2 , CH4
Toluene
Distillation sequence
Purge
Reactor
Toluene
H2 , CH4 Benzene
Diphenyl
H2 , CH4
Toluene
Separation system
Purge
Toluene
H2 , CH4
Benzene
Diphenyl
H2 , CH4
Process
Hierarchy of decisions
1- Batch Vs. Continuous
2- Input – output structure
3- Recycle structure
4- General structure of separation system:
a) Vapor recovery system
b) Liquid recovery system
5- Heat exchanger network
Advantages:
1- If the project is not profitable at any level, seek
another alternative or terminate the project
2- At each level, there are few number of alternatives
and therefore less possibility of losing an
alternative. Thus, this is a systematic way to
generate alternatives
Disadvantages:
1- It cannot be applied for batch processes (a similar
approach has been presented for batch processes by
O. Irribarren and M.F. Malone, 1985 )
2- It cannot be applied for solid or heavy polymer
process with no vapor – liquid equilibrium
Homework
Due time: two weeks
Chapter 1:
3, 4, 5, 6, 7

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Microsoft PowerPoint - Ch120884.PDF

  • 2. Conceptual Design of a chemical process Q: What is a conceptual design? A: Finding best flowsheet: 1- selecting appropriate equipment 2- best configuration of the equipment 3- determining optimum operating conditions How do we categorize the above decisions? 1 & 2 are discrete while 3 is continuous decision
  • 3. Design variables Discrete ( no. & type of reactors,…) 1- variables Continuous ( temperature, pressure,…) with local effect (reflux ratio,…) 2- variables with global effect (reactor conversion,…) Conceptual design is an MINLP optimization problem
  • 4. Hierarchical nature of process synthesis Utility system HEN Separation Reactor Design steps Outwards
  • 5. A Typical Chemical Process Hydrodealkylation of Toluene to produce Benzene (HDA) Toluene + H2 Benzene + CH4 2 Benzene Diphenyl + H2 T = 1150 – 1300 °F P = 500 psia H2 2 2 2 / Toluene @ reactor inlet / Toluene @ reactor inlet / Toluene @ reactor inlet / Toluene @ reactor inlet ≃ ≃ ≃ ≃ 5/1 5/1 5/1 5/1
  • 6. Purge Reactor Flash Toluene Col. Benzene Col. Stabilizer H2 , CH4 H2 , CH4 Benzene Diphenyl H2 , CH4 H H Toluene C Compressor A typical flowsheet
  • 7. How can we create this flowsheet ? Let’s simplify the flowsheet first: 1- remove all heat exchangers, drums and storage vessels 2- group all distillation columns 3- Simplify general structure of separation system 4- Lump complete separation system 5- Lump complete process
  • 8. Purge Reactor Flash Toluene Col. Benzene Col. Stabilizer Toluene H2 , CH4 H2 , CH4 Benzene Diphenyl H2 , CH4 Toluene
  • 9. Purge Reactor Flash Toluene H2 , CH4 H2 , CH4 Benzene Diphenyl H2 , CH4 Toluene Distillation sequence
  • 10. Purge Reactor Toluene H2 , CH4 Benzene Diphenyl H2 , CH4 Toluene Separation system
  • 12. Hierarchy of decisions 1- Batch Vs. Continuous 2- Input – output structure 3- Recycle structure 4- General structure of separation system: a) Vapor recovery system b) Liquid recovery system 5- Heat exchanger network
  • 13. Advantages: 1- If the project is not profitable at any level, seek another alternative or terminate the project 2- At each level, there are few number of alternatives and therefore less possibility of losing an alternative. Thus, this is a systematic way to generate alternatives Disadvantages: 1- It cannot be applied for batch processes (a similar approach has been presented for batch processes by O. Irribarren and M.F. Malone, 1985 ) 2- It cannot be applied for solid or heavy polymer process with no vapor – liquid equilibrium
  • 14. Homework Due time: two weeks Chapter 1: 3, 4, 5, 6, 7