This document discusses two approaches for designing a controller for non-minimum phase systems: 1) the magnitude optimum and multiple integration method, and 2) a numerical optimization approach. The magnitude optimum method uses areas calculated from the process step response to determine the PID controller parameters, eliminating the need to estimate process parameters directly. The numerical optimization approach formulates the controller design as an optimization problem to minimize sensitivity functions in the closed-loop system. Both approaches are presented as ways to design robust controllers for non-minimum phase systems.