Page 17 - Analysis, Synthesis and Design of Chemical Processes, Third Edition

B.3.1 Process Description
B.3.2 Reaction Kinetics
B.3.3 Simulation (CHEMCAD) Hints
B.3.4 References
B.4 Drying Oil Production, Unit 500
B.4.1 Process Description
B.4.2 Reaction Kinetics
B.4.3 Simulation (CHEMCAD) Hints
B.4.4 Reference
B.5 Production of Maleic Anhydride from Benzene, Unit 600

B.5.1 Process Description
B.5.2 Reaction Kinetics
B.5.3 Simulation (CHEMCAD) Hints
B.5.4 References
B.6 Ethylene Oxide Production, Unit 700
B.6.1 Process Description
B.6.2 Reaction Kinetics
B.6.3 Simulation (CHEMCAD) Hints
B.6.4 References
B.7 Formalin Production, Unit 800
B.7.1 Process Description
B.7.2 Reaction Kinetics

B.7.3 Simulation (CHEMCAD) Hints
B.7.4 References
B.8 Batch Production of L-Phenylalanine and L-Aspartic Acid, Unit 900
B.8.1 Process Description
B.8.2 Reaction Kinetics
B.8.3 References
B.9 Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene
B.9.1 Process Description
B.9.2 Reaction Kinetics and Reactor Configuration
B.9.3 Simulation (CHEMCAD) Hints
B.9.4 References
B.10 Production of Acetone via the Dehydrogenation of Isopropyl Alcohol (IPA), Unit 1100
B.10.1 Process Description
B.10.2 Reaction Kinetics
B.10.3 Simulation (CHEMCAD) Hints
B.10.4 References

B.11 Production of Heptenes from Propylene and Butenes, Unit 1200
B.11.1 Process Description
B.11.2 Reaction Kinetics
B.11.3 Simulation (CHEMCAD) Hints
B.11.4 Reference
Index