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Robust Control - $\mathcal{H}_\infty$ Synthesis
- Introduction to the Control Methodology - Model Based Control
- Some Background: From Classical Control to Robust Control
- The $\mathcal{H}_\infty$ Norm
- $\mathcal{H}_\infty$ Synthesis
- The Generalized Plant
- Problem Formulation
- Classical feedback control and closed loop transfer functions
- From a Classical Feedback Architecture to a Generalized Plant
- Modern Interpretation of the Control Specifications
- Resources
Introduction to the Control Methodology - Model Based Control
The typical methodology when applying Model Based Control to a plant is schematically shown in Figure fig:control-procedure. It consists of three steps:
- Identification or modeling: $\Longrightarrow$ mathematical model
-
Translate the specifications into mathematical criteria:
- Specifications: Response Time, Noise Rejection, Maximum input amplitude, Robustness, …
- Mathematical Criteria: Cost Function, Shape of TF
- Synthesis: research of $K$ that satisfies the specifications for the model of the system
\begin{tikzpicture}
\node[addb={+}{}{}{}{-}] (addsub) at (0, 0){};
\node[block, right=1.5 of addsub] (controller) {Controller};
\node[block, right=1.5 of controller] (plant) {Plant};
\node[block, above=1 of controller] (controller_design) {Synthesis};
\node[block, above=1 of plant] (model_plant) {Model};
\draw[<-] (addsub.west) -- ++(-1, 0) node[above right]{$r$};
\draw[->] (addsub) -- (controller.west) node[above left]{$\epsilon$};
\draw[->] (controller) -- (plant.west) node[above left]{$u$};
\draw[->] (plant.east) -- ++(1, 0) node[above left]{$y$};
\draw[] ($(plant.east) + (0.5, 0)$) -- ++(0, -1);
\draw[->] ($(plant.east) + (0.5, -1)$) -| (addsub.south);
\draw[->, dashed] (plant) -- node[midway, right, labelc, solid]{1} (model_plant);
\draw[->, dashed] (controller_design) --node[midway, right, labelc, solid]{3} (controller);
\draw[->, dashed] (model_plant) -- (controller_design);
\draw[<-, dashed] (controller_design.west) -- node[midway, above, labelc, solid]{2} ++(-1, 0) node[left, style={align=center}]{Specifications};
\end{tikzpicture}
In this document, we will mainly focus on steps 2 and 3.
Some Background: From Classical Control to Robust Control
Classical Control (1930)
-
Tools:
- TF (input-output)
- Nyquist, Bode, Black, \ldots
- P-PI-PID, Phase lead-lag, \ldots
-
Advantages:
- Stability
- Performances
- Robustness
-
Disadvantages:
- Manual Method
- Only SISO
Modern Control (1960)
-
Tools:
- State Space
- Optimal Command
- LQR, LQG
-
Advantages:
- Automatic Synthesis
- MIMO
- Optimisation problem
-
Disadvantages:
- Robustness
- Rejection of Perturbations
Robust Control (1980)
-
Tools:
- Disk Margin
- Systems and Signals norms ($\mathcal{H}_\infty$ and $\mathcal{H}_2$ norms)
- Closed Loop Transfer Functions
- Loop Shaping
-
Advantages:
- Stability
- Performances
- Robustness
- Automatic Synthesis
- MIMO
- Optimization Problem
-
Disadvantages:
- Requires the knowledge of specific tools
- Need a reasonably good model of the system
The $\mathcal{H}_\infty$ Norm
The $\mathcal{H}_\infty$ norm is defined as the peak of the maximum singular value of the frequency response
\begin{equation} \|G(s)\|_\infty = \max_\omega \bar{\sigma}\big( G(j\omega) \big) \end{equation}For a SISO system $G(s)$, it is simply the peak value of $|G(j\omega)|$ as a function of frequency:
\begin{equation} \|G(s)\|_\infty = \max_{\omega} |G(j\omega)| \label{eq:hinf_norm_siso} \end{equation}Let's define a plant dynamics:
w0 = 2*pi; k = 1e6; xi = 0.04;
G = 1/k/(s^2/w0^2 + 2*xi*s/w0 + 1);
And compute its $\mathcal{H}_\infty$ norm using the hinfnorm
function:
hinfnorm(G)
1.0013e-05
The magnitude $|G(j\omega)|$ of the plant $G(s)$ as a function of frequency is shown in Figure fig:hinfinity_norm_siso_bode. The maximum value of the magnitude over all frequencies does correspond to the $\mathcal{H}_\infty$ norm of $G(s)$ as Equation eqref:eq:hinf_norm_siso implies.
$\mathcal{H}_\infty$ Synthesis
Optimization problem: $\hinf$ synthesis is a method that uses an algorithm (LMI optimization, Riccati equation) to find a controller of the same order as the system so that the $\hinf$ norms of defined transfer functions are minimized.
Engineer work:
- Write the problem as standard $\hinf$ problem
- Translate the specifications as $\hinf$ norms
- Make the synthesis and analyze the obtain controller
- Reduce the order of the controller for implementation
Many ways to use the $\hinf$ Synthesis:
- Traditional $\hinf$ Synthesis
- Mixed Sensitivity Loop Shaping
- Fixed-Structure $\hinf$ Synthesis
- Signal Based $\hinf$ Synthesis
The Generalized Plant
\begin{tikzpicture}
\node[block={2.0cm}{2.0cm}] (P) {$P$};
\node[above] at (P.north) {Generalized Plant};
% Input and outputs coordinates
\coordinate[] (inputw) at ($(P.south west)!0.75!(P.north west)$);
\coordinate[] (inputu) at ($(P.south west)!0.25!(P.north west)$);
\coordinate[] (outputz) at ($(P.south east)!0.75!(P.north east)$);
\coordinate[] (outputv) at ($(P.south east)!0.25!(P.north east)$);
% Connections and labels
\draw[<-] (inputw) -- ++(-0.8, 0) node[above right]{$w$};
\draw[<-] (inputu) -- ++(-0.8, 0) node[above right]{$u$};
\draw[->] (outputz) -- ++(0.8, 0) node[above left]{$z$};
\draw[->] (outputv) -- ++(0.8, 0) node[above left]{$v$};
\end{tikzpicture}
Notation | Meaning |
---|---|
$P$ | Generalized plant model |
$w$ | Exogenous inputs: commands, disturbances, noise |
$z$ | Exogenous outputs: signals to be minimized |
$v$ | Controller inputs: measurements |
$u$ | Control signals |
Problem Formulation
The $\mathcal{H}_\infty$ Synthesis objective is to find all stabilizing controllers $K$ which minimize
\begin{equation} \| F_l(P, K) \|_\infty = \max_{\omega} \overline{\sigma} \big( F_l(P, K)(j\omega) \big) \end{equation} \begin{tikzpicture}
% Blocs
\node[block={2.0cm}{2.0cm}] (P) {$P$};
\node[block={1.5cm}{1.5cm}, below=0.7 of P] (K) {$K$};
% Input and outputs coordinates
\coordinate[] (inputw) at ($(P.south west)!0.75!(P.north west)$);
\coordinate[] (inputu) at ($(P.south west)!0.25!(P.north west)$);
\coordinate[] (outputz) at ($(P.south east)!0.75!(P.north east)$);
\coordinate[] (outputv) at ($(P.south east)!0.25!(P.north east)$);
% Connections and labels
\draw[<-] (inputw) node[above left, align=right]{(weighted)\\exogenous inputs\\$w$} -- ++(-1.5, 0);
\draw[<-] (inputu) -- ++(-0.8, 0) |- node[left, near start, align=right]{control signals\\$u$} (K.west);
\draw[->] (outputz) node[above right, align=left]{(weighted)\\exogenous outputs\\$z$} -- ++(1.5, 0);
\draw[->] (outputv) -- ++(0.8, 0) |- node[right, near start, align=left]{sensed output\\$v$} (K.east);
\end{tikzpicture}
Classical feedback control and closed loop transfer functions
\begin{tikzpicture}
\node[addb={+}{}{}{}{-}] (addfb) at (0, 0){};
\node[block, right=0.8 of addfb] (K){$K(s)$};
\node[addb={+}{}{}{}{}, right=0.8 of K] (addu){};
\node[block, right=0.8 of addu] (G){$G(s)$};
\draw[<-] (addfb.west) -- ++(-0.8, 0) node[above right]{$r$};
\draw[->] (addfb.east) -- (K.west) node[above left]{$\epsilon$};
\draw[->] (K.east) -- (addu.west) node[above left]{$u$};
\draw[->] (addu.east) -- (G.west);
\draw[<-] (addu.north) -- ++(0, 0.8) node[below right]{$d$};
\draw[->] (G.east) -- ++(1.2, 0);
\draw[->] ($(G.east) + (0.6, 0)$) node[branch]{} node[above]{$y$} -- ++(0, -0.8) -| (addfb.south);
\end{tikzpicture}
Notation | Meaning |
---|---|
$G$ | Plant model |
$K$ | Controller |
$r$ | Reference inputs |
$y$ | Plant outputs |
$u$ | Control signals |
$d$ | Input Disturbance |
$\epsilon$ | Tracking Error |
From a Classical Feedback Architecture to a Generalized Plant
The procedure is:
- define signals of the generalized plant
- Remove $K$ and rearrange the inputs and outputs
\begin{tikzpicture}
\node[addb={+}{}{}{}{-}] (addfb) at (0, 0){};
\node[block, right=0.8 of addfb] (K){$K(s)$};
\node[block, right=0.8 of K] (G){$G(s)$};
\draw[<-] (addfb.west) -- ++(-0.8, 0) node[above right]{$r$};
\draw[->] (addfb.east) -- (K.west) node[above left]{$\epsilon$};
\draw[->] (K.east) -- (G.west) node[above left]{$u$};
\draw[->] (G.east) -- ++(1.2, 0);
\draw[->] ($(G.east) + (0.6, 0)$) node[branch]{} node[above]{$y$} -- ++(0, -0.8) -| (addfb.south);
\end{tikzpicture}
\begin{tikzpicture}
\node[block] (G) {$G(s)$};
\node[addb={+}{-}{}{}{}, right=0.6 of G] (addw) {};
\coordinate[above right=0.6 and 1.4 of addw] (u);
\coordinate[above=0.6 of u] (epsilon);
\coordinate[] (w) at ($(epsilon-|G.west)+(-1.4, 0)$);
\node[block, below left=0.8 and 0 of addw] (K) {$K(s)$};
% Connections
\draw[->] (G.east) -- (addw.west);
\draw[->] ($(addw.east)+(0.4, 0)$)node[branch]{} |- (epsilon) node[above left](z1){$\epsilon$};
\draw[->] ($(G.west)+(-0.4, 0)$)node[branch](start){} |- (u) node[above left](z2){$u$};
\draw[->] (addw.east) -- (addw-|z1) |- node[near start, right]{$v$} (K.east);
\draw[->] (K.west) -| node[near end, left]{$u$} ($(G-|w)+(0.4, 0)$) -- (G.west);
\draw[->] (w) node[above]{$w = r$} -| (addw.north);
\draw [decoration={brace, raise=5pt}, decorate] (z1.north east) -- node[right=6pt]{$z$} (z2.south east);
\begin{scope}[on background layer]
\node[fit={(G.south-|start.west) ($(z1.north west)+(-0.4, 0)$)}, inner sep=6pt, draw, dashed, fill=black!20!white] (P) {};
\node[below right] at (P.north west) {Generalized Plant $P(s)$};
\end{scope}
\end{tikzpicture}
Let's find the Generalized plant of corresponding to the tracking control architecture shown in Figure fig:classical_feedback_tracking
First, define the signals of the generalized plant:
- Exogenous inputs: $w = r$
- Signals to be minimized: $z_1 = \epsilon$, $z_2 = u$
- Control signals: $v = y$
- Control inputs: $u$
Then, Remove $K$ and rearrange the inputs and outputs. We obtain the generalized plant shown in Figure fig:mixed_sensitivity_ref_tracking.
Using Matlab, the generalized plant can be defined as follows:
P = [1 -G;
0 1;
1 -G]
Modern Interpretation of the Control Specifications
Introduction
-
Reference tracking Overshoot, Static error, Setling time
- $S(s) = T_{r \rightarrow \epsilon}$
-
Disturbances rejection
- $G(s) S(s) = T_{d \rightarrow \epsilon}$
-
Measurement noise filtering
- $T(s) = T_{n \rightarrow \epsilon}$
-
Small command amplitude
- $K(s) S(s) = T_{r \rightarrow u}$
-
Stability
- $S(s)$, $T(s)$, $K(s)S(s)$, $G(s)S(s)$
- Robustness to plant uncertainty (stability margins)
- Controller implementation
**
Resources
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yt:?listType=playlist&list=PLsjPUqcL7ZIFHCObUU_9xPUImZ203gB4o