Chemical Reaction Engineering Chapter 3 Part 3 Reaction

Chemical Reaction Engineering Chapter 3, Part 3: Reaction Stoichiometry: Flow

Flow System Stoichiometric Table Species Symbol A Initial Change Remaining A ____________

Flow System Stoichiometric Table Species Symbol A A B B Initial ____ Change Remaining ______

Flow System Stoichiometric Table Species Symbol A A B B C C Initial ____ Change Remaining ______

Flow System Stoichiometric Table Species Symbol A A B B C C D D Initial ____ Change Remaining ______

Flow System Stoichiometric Table Species Symbol A A B B C C D D Inert I Initial ____ Change Remaining ______

Flow System Stoichiometric Table Species Symbol A A B B C C D D Inert I Initial Change ______ where Remaining and

Concentration: Flow System • Flow Stystem:

Concentration: Flow System • Flow Stystem: • Liquid Phase Flow System: etc.

Concentration: Liquid Flow System • Flow Stystem: • Liquid Phase Flow System: etc. If the rate of reaction were then we would have This gives us -r. A = f(X). Consequently, we can use the methods discussed in Chapter 2 to size a large number of reactors, either alone or in series.

Concentration: Gas Flow System

Concentration: Gas Flow System

Concentration: Gas Flow System

Concentration: Gas Flow System etc.

Concentration: Gas Flow System etc. Again, these equations give us information about -r. A = f(X), which we can use to size reactors. For example if the gas phase reaction has the rate law

Concentration: Gas Flow System etc. Again, these equations give us information about -r. A = f(X), which we can use to size reactors. For example if the gas phase reaction has the rate law then with