If a reaction is conducted in a batch reactor, then time, required to achieve conversion XA, can be found as
and integrated solutions for a variety of reaction-types are provided below:
Batch Reactor, Constant Pressure:
Zero order reaction: -rA = k
First order reaction: -rA = kCA
Second order reaction: -rA = kCA2
Third order reaction: -rA = kCA3
Second order reaction: -rA = kCACB
Third order reaction: -rA = kCA2CB
Third order: -rA = kCACB2
Batch Reactor (Plug Flow Reactor), Constant Density:
For a constant volume case, ε = 0 and Equation 1.25 reduces to the following design equation
And integrated solutions are provided below:
Zero order reaction: -rA = k
First order reaction: -rA = kCA
Second order reaction: -rA = kCA2
Third order reaction: -rA = kCA3
Second order reaction: -rA = kCACB
Third order: -rA = kCA2CB
Third order: -rA = kCACB2
Third order: -rA = kCACBCC