In the context of a second-order irreversible reaction A + B → C occurring in a series of three tank reactors with varying holdup volumes, a dynamic model for transient operation can be formulated.
Assuming excess B, with initial concentrations CAo and CBo for A and B, and a steady-state flow rate U m³/hr, the system's dynamic behavior can be described.
By deriving the load transfer function, one can analyze how changes in the initial concentration of reactant A impact the system. Specifically, investigating the system's response to a unit step change in A's concentration provides valuable insights into the reactors' transient behavior and facilitates process optimization.