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Single reactions Isothermal condition (T=623K) Isobaric condition (P=2bar) Propylene (C 3 H 6 ) as limiting reactant Oxygen (O 2 ) in excess Non-elementary reaction Non-reversible reaction First order reaction at Basic Design Assumption

Basic Design Assumption

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C3H6 (g) + NH3 (g) + 9/4 O2 (g) C2H3N (g) + 3H2O (g) + 1/2 CO2 (g) + 1/2 CO (g)

Single reactions Isothermal condition (T=623K) Isobaric condition (P=2bar) Propylene (C3H6) as limiting reactant Oxygen (O2) in excess Non-elementary reaction Non-reversible reaction First order reaction at k=0.01744 s-1Basic Design AssumptionFirst Order ReactionVolume of PFRConversion, XFAo/-rANUMERICAL METHODS AND OPTIMIZATION

Excel representation of Chemical Reaction Engineering calculation.

Matlab representation of the calculation to plot the first order reaction graph.

Graph of First Order Reaction.Simpsons 3/8 Rule.

TRAPEZOIDAL RULE