chemical reaction engineering chapter 4, part 1: applying the algorithm to a cstr

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Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

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Page 1: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Chemical Reaction Engineering

Chapter 4, Part 1:

Applying the Algorithm to a CSTR

Page 2: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Summary

At the start of the chapter we saw we needed -rA=f(X). This result is achieved in two steps.

1. Rate Laws

– -rA=k f(Ci)

– 1st order A--> B or 1st order

– 2nd order A+B --> C

– Rate laws are found by experiment

2. Stoichiometry

– Liquid:

– Gas:

-rA=kCA

rA k C A C B

KC

-rA=kACACB

C A CA 0 1 X

C A CA 0 1 X

1 X PP0

T0

T

C A CT 0

FT

FT 0

PP0

T0

T

Page 3: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

Page 4: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

The Evaluate step can be carried out:

Page 5: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

The Evaluate step can be carried out:1. Graphically (Chapter 2 plots)

Page 6: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

The Evaluate step can be carried out:1. Graphically (Chapter 2 plots)

2. Numerically (Quadrature formulas: Chapter 2 and Appendices)

Page 7: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

The Evaluate step can be carried out:1. Graphically (Chapter 2 plots)

2. Numerically (Quadrature formulas: Chapter 2 and Appendices)

3. Analytically (Integral tables in Appendix)

Page 8: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Algorithm for Isothermal Reactor Design

1. Mole Balance and Design Equation

2. Rate Law

3. Stoichiometry

4. Combine

5. Evaluate

The Evaluate step can be carried out:1. Graphically (Chapter 2 plots)

2. Numerically (Quadrature formulas: Chapter 2 and Appendices)

3. Analytically (Integral tables in Appendix)

4. Software packages (Appendix - Polymath)

Page 9: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 10: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 11: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 12: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 13: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 14: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 15: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 16: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Page 17: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Page 18: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Page 19: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Page 20: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Stoichiometry: gas phase, isothermal (T=T0), no pressure drop (P=P0)

French Menu Analogy

Page 21: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Remember the French Menu reaction:

For a gas phase system:

Deriving CA and CB:

Page 22: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Remember the French Menu reaction:

For a gas phase system:

If the conditions are isothermal (T = T0) and isobaric (P =P0):

Deriving CA and CB:

Page 23: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Remember the French Menu reaction:

For a gas phase system:

If the conditions are isothermal (T = T0) and isobaric (P =P0):

We must divide by the stoichiometric coefficient of our basis of calculation yielding:

Deriving CA and CB:

Page 24: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

Remember the French Menu reaction:

For a gas phase system:

If the conditions are isothermal (T = T0) and isobaric (P =P0):

We must divide by the stoichiometric coefficient of our basis of calculation yielding:

And if the feed is equal molar, then:

Deriving CA and CB:

Page 25: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

This leaves us with CA as a function of conversion alone:

Deriving CA and CB:

Page 26: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

French Menu Analogy

This leaves us with CA as a function of conversion alone:

Similarly for CB:

FB0 FA0

Therefore, B 1

Deriving CA and CB:

Page 27: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Stoichiometry: gas phase, isothermal (T=T0), no pressure drop (P=P0)

[Why do you think CB is constant, when B is consumed?]

French Menu Analogy

Page 28: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Stoichiometry: gas phase, isothermal (T=T0), no pressure drop (P=P0)

[Why do you think CB is constant, when B is consumed?]

French Menu Analogy

Page 29: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Stoichiometry: gas phase, isothermal (T=T0), no pressure drop (P=P0)

[Why do you think CB is constant, when B is consumed?]

Combine:

French Menu Analogy

Page 30: Chemical Reaction Engineering Chapter 4, Part 1: Applying the Algorithm to a CSTR

Example: The elementary gas phase reaction takes place in a CSTR at constant temperature (500 K) and constant pressure (16.4 atm). The feed is equal molar in A and B.

Mole Balance:

Rate Law:

Stoichiometry: gas phase, isothermal (T=T0), no pressure drop (P=P0)

[Why do you think CB is constant, when B is consumed?]

Combine:

Evaluate:

French Menu Analogy