Type: Object Data: A, B, C, D, and E matrices Inputs: Input (u) Outputs: States (x), Output (y) Description: LTI State Space Model APMonitor Usage: sys = lti GEKKO Usage: x,y,u = m.state_space(A,B,C,D=None) Other optional arguments: E=None,discrete=False,dense=False
Linear Time Invariant (LTI) state space models are a linear representation of a dynamic system in either discrete or continuous time. Putting a model into state space form is the basis for many methods in process dynamics and control analysis. Below is the continuous time form of a model in state space form.
$$E\dot x = A x + B u$$
$$y = C x + D u$$
with states `x in \mathbb{R}^n` and state derivatives `\dot x = {dx}/{dt} in \mathbb{R}^n`. The notation `in \mathbb{R}^n` means that `x` and `\dot x` are in the set of real-numbered vectors of length `n`. The other elements are the outputs `y in \mathbb{R}^p`, the inputs `u in \mathbb{R}^m`, the state transition matrix `A`, the input matrix `B`, and the output matrix `C`. The remaining matrix `D` is typically zeros because the inputs do not typically affect the outputs directly. The dimensions of each matrix are shown below with `m` inputs, `n` states, and `p` outputs.
$$A \in \mathbb{R}^{n \, \mathrm{x} \, n}$$ $$B \in \mathbb{R}^{n \, \mathrm{x} \, m}$$ $$C \in \mathbb{R}^{p \, \mathrm{x} \, n}$$ $$D \in \mathbb{R}^{p \, \mathrm{x} \, m}$$ $$E \in \mathbb{R}^{n \, \mathrm{x} \, n}$$
Model Predictive Control, or MPC, is an advanced method of process control that has been in use in the process industries such as chemical plants and oil refineries since the 1980s. Model predictive controllers rely on dynamic models of the process, most often linear empirical models obtained by system identification.
These models are typically in the finite impulse response form or linear state space form. Either model form can be converted to an APMonitor for a linear MPC upgrade. Once in APMonitor form, nonlinear elements can be added to avoid multiple model switching, gain scheduling, or other ad hoc measures commonly employed because of linear MPC restrictions.
! new linear time-invariant object Model control Objects mpc = lti End Objects End Model ! Model information ! continuous form ! dx/dt = A * x + B * u ! y = C * x + D * u ! ! dimensions ! (nx1) = (nxn)*(nx1) + (nxm)*(mx1) ! (px1) = (pxn)*(nx1) + (pxm)*(mx1) ! ! discrete form ! x[k+1] = A * x[k] + B * u[k] ! y[k] = C * x[k] + D * u[k] File mpc.txt sparse, continuous ! dense/sparse, continuous/discrete 2 ! m=number of inputs 3 ! n=number of states 3 ! p=number of outputs End File ! A matrix (row, column, value) File mpc.a.txt 1 1 0.9 2 2 0.1 3 3 0.5 End File ! B matrix (row, column, value) File mpc.b.txt 1 1 1.0 2 2 1.0 3 1 0.5 3 2 0.5 End File ! C matrix (row, column, value) File mpc.c.txt 1 1 0.5 2 2 1.0 3 3 2.0 End File ! D matrix (row, column, value) File mpc.d.txt 1 1 0.2 End File
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