Sensor Fusion Paper - Computation with Matlab

Table of Contents

The control architecture studied here is shown on figure 1 where:

sf_arch_class_prefilter.png

Figure 1: Control Architecture

Here is the outline of the matlab analysis for this control architecture:

All the files (data and Matlab scripts) are accessible here.

1 Definition of the plant

The studied system consists of a solid positioned on top of a motorized uni-axial soft suspension.

The absolute position \(x\) of the solid is measured using an inertial sensor and a force \(F\) can be applied to the mass using a voice coil actuator.

The model of the system is represented on figure 2 where the mass of the solid is \(m = 20\ [kg]\), the stiffness of the suspension is \(k = 10^4\ [N/m]\) and the damping of the system is \(c = 10^2\ [N/(m/s)]\).

mech_sys_alone.png

Figure 2: One degree of freedom system

The plant \(G\) is defined on matlab and its bode plot is shown on figure 3.

m = 20;  % [kg]
k = 1e4; % [N/m]
c = 1e2; % [N/(m/s)]

G = 1/(m*s^2 + c*s + k);

bode_plot_mech_sys.png

Figure 3: Bode plot of \(G\) (png, pdf)

2 Multiplicative input uncertainty

We choose to use the multiplicative input uncertainty to model the plant uncertainty: \[ \Pi_I: \ G^\prime(s) = G(s) (1 + w_I(s) \Delta(s)),\text{ with } |\Delta(j\omega)| < 1 \ \forall \omega \]

The uncertainty weight \(w_I\) has the following form: \[ w_I(s) = \frac{\tau s + r_0}{(\tau/r_\infty) s + 1} \] where \(r_0=0.1\) is the relative uncertainty at steady-state, \(1/\tau=80\text{Hz}\) is the frequency at which the relative uncertainty reaches 100%, and \(r_\infty=10\) is the magnitude of the weight at high frequency.

We defined the uncertainty weight on matlab. Its bode plot is shown on figure 4.

r0 = 0.1;
rinf = 10;
tau = 1/2/pi/80;

wI = (tau*s + r0)/((tau/rinf)*s+1);

bode_wi.png

Figure 4: Bode plot of \(w_I\) (png, pdf)

The uncertain model is created with the ultidyn function. Elements in the uncertainty set \(\Pi_I\) are computed and their bode plot is shown on figure 5.

Delta = ultidyn('Delta', [1 1]);

Gd = G*(1+wI*Delta);
Gds = usample(Gd, 20);

plant_uncertainty_bode_plot.png

Figure 5: Some elements in the uncertainty set \(\Pi_I\) (png, pdf)

3 Specifications and performance weights

The control objective is to isolate the displacement \(x\) of the mass from the ground motion \(w\).

The specifications are described below:

  • at least a factor \(10\) of disturbance rejection at \(2\ \text{Hz}\) and with a slope of \(2\) below \(2\ \text{Hz}\) until a rejection of \(10^3\)
  • the noise attenuation should be at least \(10\) above \(100\ \text{Hz}\) and with a slope of \(-2\) above

These specifications can be represented as upper bounds on the closed loop transfer functions \(S\) and \(T\) (see figure 6).

bode_requirements.png

Figure 6: Upper bounds on \(S\) and \(T\) (png, pdf)

We now define two weights, \(w_S(s)\) and \(w_T(s)\) such that \(1/|w_S|\) and \(1/|w_T|\) are lower than the previously defined upper bounds. Then, the performance specifications are satisfied if the following condition is valid: \[ \big|S(j\omega)\big| < \frac{1}{|w_S(j\omega)|} ; \quad \big|T(j\omega)\big| < \frac{1}{|w_T(j\omega)|}, \quad \forall \omega \]

The weights are defined as follow. They magnitude is compared with the upper bounds on \(S\) and \(T\) on figure 7.

wS = 1600/(s+0.13)^2;
wT = 1000*((s/(2*pi*1000)))^2;

compare_weights_upper_bounds_S_T.png

Figure 7: Weights \(w_S\) and \(w_T\) with the upper bounds on \(S\) and \(T\) obtained from the specifications (png, pdf)

4 Upper bounds on the norm of the complementary filters for NP, RS and RP

Now that we have defined \(w_I\), \(w_S\) and \(w_T\), we can derive conditions for Nominal Performance, Robust Stability and Robust Performance (\(j\omega\) is omitted here for readability):

\begin{align*} \text{NP} &\Leftrightarrow |H_H| < \frac{1}{|w_S|} \text{ and } |H_L| < \frac{1}{|w_T|} \quad \forall \omega \\ \text{RS} &\Leftrightarrow |H_L| < \frac{1}{|w_I| (2 + |w_I|)} \quad \forall \omega \\ \text{RP for } S &\Leftarrow |H_H| < \frac{1 + |w_I|}{|w_S| (2 + |w_I|)} \quad \forall \omega \\ \text{RP for } T &\Leftrightarrow |H_L| < \frac{1}{|w_T| (1 + |w_I|) + |w_I|} \quad \forall \omega \end{align*}

These conditions are upper bounds on the complementary filters used for control.

We plot these conditions on figure 8.

weights_NP_RS_RP.png

Figure 8: Upper bounds on the norm of the complementary filters for NP, RS and RP (png, pdf)

5 H-Infinity synthesis of complementary filters

We here synthesize the complementary filters using the \(\mathcal{H}_\infty\) synthesis. The goal is to specify upper bounds on the norms of \(H_L\) and \(H_H\) while ensuring their complementary property (\(H_L + H_H = 1\)).

In order to do so, we use the generalized plant shown on figure 9 where \(w_L\) and \(w_H\) weighting transfer functions that will be used to shape \(H_L\) and \(H_H\) respectively.

sf_hinf_filters_plant_b.png

Figure 9: Generalized plant used for the \(\mathcal{H}_\infty\) synthesis of the complementary filters

The \(\mathcal{H}_\infty\) synthesis applied on this generalized plant will give a transfer function \(H_L\) (figure 10) such that the \(\mathcal{H}_\infty\) norm of the transfer function from \(w\) to \([z_H,\ z_L]\) is less than one: \[ \left\| \begin{array}{c} H_L w_L \\ (1 - H_L) w_H \end{array} \right\|_\infty < 1 \]

Thus, if the above condition is verified, we can define \(H_H = 1 - H_L\) and we have that: \[ \left\| \begin{array}{c} H_L w_L \\ H_H w_H \end{array} \right\|_\infty < 1 \] Which is almost (with an maximum error of \(\sqrt{2}\)) equivalent to:

\begin{align*} |H_L| &< \frac{1}{|w_L|}, \quad \forall \omega \\ |H_H| &< \frac{1}{|w_H|}, \quad \forall \omega \end{align*}

We then see that \(w_L\) and \(w_H\) can be used to shape both \(H_L\) and \(H_H\) while ensuring (by definition of \(H_H = 1 - H_L\)) their complementary property.

sf_hinf_filters_b.png

Figure 10: \(\mathcal{H}_\infty\) synthesis of the complementary filters

Thus, if we choose \(w_L\) and \(w_H\) such that \(1/|w_L|\) and \(1/|w_H|\) lie below the upper bounds of figure 8, we will ensure the NP, RS and RP of the controlled system.

Depending if we are interested only in NP, RS or RP, we can adjust the weights \(w_L\) and \(w_H\).

omegab = 2*pi*9;
wH = (omegab)^2/(s + omegab*sqrt(1e-5))^2;
omegab = 2*pi*28;
wL = (s + omegab/(4.5)^(1/3))^3/(s*(1e-4)^(1/3) + omegab)^3;

weights_wl_wh.png

Figure 11: Weights on the complementary filters \(w_L\) and \(w_H\) and the associated performance weights (png, pdf)

We define the generalized plant \(P\) on matlab.

P = [0   wL;
     wH -wH;
     1   0];

And we do the \(\mathcal{H}_\infty\) synthesis using the hinfsyn command.

[Hl_hinf, ~, gamma, ~] = hinfsyn(P, 1, 1,'TOLGAM', 0.001, 'METHOD', 'ric', 'DISPLAY', 'on');
[Hl_hinf, ~, gamma, ~] = hinfsyn(P, 1, 1,'TOLGAM', 0.001, 'METHOD', 'ric', 'DISPLAY', 'on');
Test bounds:      0.0000 <  gamma  <=      1.7285

  gamma    hamx_eig  xinf_eig  hamy_eig   yinf_eig   nrho_xy   p/f
    1.729   4.1e+01   8.4e-12   1.8e-01    0.0e+00    0.0000    p
    0.864   3.9e+01 -5.8e-02#  1.8e-01    0.0e+00    0.0000    f
    1.296   4.0e+01   8.4e-12   1.8e-01    0.0e+00    0.0000    p
    1.080   4.0e+01   8.5e-12   1.8e-01    0.0e+00    0.0000    p
    0.972   3.9e+01 -4.2e-01#  1.8e-01    0.0e+00    0.0000    f
    1.026   4.0e+01   8.5e-12   1.8e-01    0.0e+00    0.0000    p
    0.999   3.9e+01   8.5e-12   1.8e-01    0.0e+00    0.0000    p
    0.986   3.9e+01 -1.2e+00#  1.8e-01    0.0e+00    0.0000    f
    0.993   3.9e+01 -8.2e+00#  1.8e-01    0.0e+00    0.0000    f
    0.996   3.9e+01   8.5e-12   1.8e-01    0.0e+00    0.0000    p
    0.994   3.9e+01   8.5e-12   1.8e-01    0.0e+00    0.0000    p
    0.993   3.9e+01 -3.2e+01#  1.8e-01    0.0e+00    0.0000    f

 Gamma value achieved:     0.9942

We then define the high pass filter \(H_H = 1 - H_L\). The bode plot of both \(H_L\) and \(H_H\) is shown on figure 12.

Hh_hinf = 1 - Hl_hinf;

hinf_filters_results.png

Figure 12: Obtained complementary filters using \(\mathcal{H}_\infty\) synthesis (png, pdf)

6 Complementary filters using analytical formula

We here use analytical formula for the complementary filters \(H_L\) and \(H_H\).

The first two formulas that are used to generate complementary filters are:

\begin{align*} H_L(s) &= \frac{(1+\alpha) (\frac{s}{\omega_0})+1}{\left((\frac{s}{\omega_0})+1\right) \left((\frac{s}{\omega_0})^2 + \alpha (\frac{s}{\omega_0}) + 1\right)}\\ H_H(s) &= \frac{(\frac{s}{\omega_0})^2 \left((\frac{s}{\omega_0})+1+\alpha\right)}{\left((\frac{s}{\omega_0})+1\right) \left((\frac{s}{\omega_0})^2 + \alpha (\frac{s}{\omega_0}) + 1\right)} \end{align*}

where:

  • \(\omega_0\) is the blending frequency in rad/s.
  • \(\alpha\) is used to change the shape of the filters:
    • Small values for \(\alpha\) will produce high magnitude of the filters \(|H_L(j\omega)|\) and \(|H_H(j\omega)|\) near \(\omega_0\) but smaller value for \(|H_L(j\omega)|\) above \(\approx 1.5 \omega_0\) and for \(|H_H(j\omega)|\) below \(\approx 0.7 \omega_0\)
    • A large \(\alpha\) will do the opposite

This is illustrated on figure 13. As it is usually wanted to have the \(\| S \|_\infty < 2\), \(\alpha\) between \(0.5\) and \(1\) gives a good trade-off between the performance and the robustness. The slope of those filters at high and low frequencies is \(-2\) and \(2\) respectively for \(H_L\) and \(H_H\).

comp_filters_param_alpha.png

Figure 13: Effect of the parameter \(\alpha\) on the shape of the generated second order complementary filters (png, pdf)

The parameters \(\alpha\) and \(\omega_0\) are chosen in order to have that the complementary filters stay below the defined upper bounds.

The obtained complementary filters are shown on figure 14. The Robust Performance is not fulfilled for \(T\), and we see that the RP condition as a slop of \(-3\). We thus have to use different formula for the complementary filters here.

w0 = 2*pi*13;
alpha = 0.8;

Hh2_ana = (s/w0)^2*((s/w0)+1+alpha)/(((s/w0)+1)*((s/w0)^2 + alpha*(s/w0) + 1));
Hl2_ana = ((1+alpha)*(s/w0)+1)/(((s/w0)+1)*((s/w0)^2 + alpha*(s/w0) + 1));

complementary_filters_second_order.png

Figure 14: Second order complementary filters using the analytical formula (png, pdf)

The following formula gives complementary filters with slopes of \(-3\) and \(3\):

\begin{align*} H_L(s) &= \frac{\left(1+(\alpha+1)(\beta+1)\right) (\frac{s}{\omega_0})^2 + (1+\alpha+\beta)(\frac{s}{\omega_0}) + 1}{\left(\frac{s}{\omega_0} + 1\right) \left( (\frac{s}{\omega_0})^2 + \alpha (\frac{s}{\omega_0}) + 1 \right) \left( (\frac{s}{\omega_0})^2 + \beta (\frac{s}{\omega_0}) + 1 \right)}\\ H_H(s) &= \frac{(\frac{s}{\omega_0})^3 \left( (\frac{s}{\omega_0})^2 + (1+\alpha+\beta) (\frac{s}{\omega_0}) + (1+(\alpha+1)(\beta+1)) \right)}{\left(\frac{s}{\omega_0} + 1\right) \left( (\frac{s}{\omega_0})^2 + \alpha (\frac{s}{\omega_0}) + 1 \right) \left( (\frac{s}{\omega_0})^2 + \beta (\frac{s}{\omega_0}) + 1 \right)} \end{align*}

The parameters are:

  • \(\omega_0\) is the blending frequency in rad/s
  • \(\alpha\) and \(\beta\) that are used to change the shape of the filters similarly to the parameter \(\alpha\) for the second order complementary filters

The filters are defined below and the result is shown on figure 15 where we can see that the complementary filters are below the defined upper bounds.

alpha = 1;
beta = 10;
w0 = 2*pi*14;

Hh3_ana = (s/w0)^3 * ((s/w0)^2 + (1+alpha+beta)*(s/w0) + (1+(alpha+1)*(beta+1)))/((s/w0 + 1)*((s/w0)^2+alpha*(s/w0)+1)*((s/w0)^2+beta*(s/w0)+1));
Hl3_ana = ((1+(alpha+1)*(beta+1))*(s/w0)^2 + (1+alpha+beta)*(s/w0) + 1)/((s/w0 + 1)*((s/w0)^2+alpha*(s/w0)+1)*((s/w0)^2+beta*(s/w0)+1));

complementary_filters_third_order.png

Figure 15: Third order complementary filters using the analytical formula (png, pdf)

7 Comparison of complementary filters

The generated complementary filters using \(\mathcal{H}_\infty\) and the analytical formulas are compared on figure 16.

Although they are very close to each other, there is some difference to note here:

  • the analytical formula provides a very simple way to generate the complementary filters (and thus the controller), they could even be used to tune the controller online using the parameters \(\alpha\) and \(\omega_0\). However, these formula have the property that \(|H_H|\) and \(|H_L|\) are symmetrical with the frequency \(\omega_0\) which may not be desirable.
  • while the \(\mathcal{H}_\infty\) synthesis of the complementary filters is not as straightforward as using the analytical formula, it provides a more optimized procedure to obtain the complementary filters

The complementary filters obtained with the \(\mathcal{H}_\infty\) will be used for further analysis.

comp_hinf_analytical.png

Figure 16: Comparison of the complementary filters obtained with \(\mathcal{H}_\infty\) synthesis and with the analytical formula (png, pdf)

8 Controller Analysis

The controller \(K\) is computed from the plant model \(G\) and the low pass filter \(H_H\): \[ K = G^{-1} H_H^{-1} \]

As this is not proper and thus realizable, a second order low pass filter is added with a crossover frequency much larger than the control bandwidth.

omega = 2*pi*1000;
K = 1/(Hh_hinf*G) * 1/((1+s/omega)*(1+s/omega+(s/omega)^2));
zpk(K)

ans =

        4.961e12 (s+9.915e04) (s^2 + 5s + 500) (s^2 + 284.6s + 2.135e04) (s^2 + 130.5s + 9887)
  --------------------------------------------------------------------------------------------------
  (s+9.914e04) (s+6283) (s^2 + 0.3576s + 0.03198) (s^2 + 413.8s + 6.398e04) (s^2 + 6283s + 3.948e07)

Continuous-time zero/pole/gain model.

The bode plot of the controller is shown on figure 17:

  • two integrator are present at low frequency
  • the resonance of the plant at \(3.5\ \text{Hz}\) is inverted (notched)
  • a lead is added at \(10\ \text{Hz}\)

bode_plot_controller.png

Figure 17: Bode plot of the obtained controller \(K\) (png, pdf)

9 Nominal Stability and Nominal Performance

The nominal stability of the system is first checked with the allmargin matlab command.

allmargin(K*G*Hl_hinf)
allmargin(K*G*Hl_hinf)
ans =
  struct with fields:

     GainMargin: 4.46426896164391
    GMFrequency: 243.854595348016
    PhaseMargin: 35.7045152899792
    PMFrequency: 88.3664383511655
    DelayMargin: 0.00705201387841809
    DMFrequency: 88.3664383511655
         Stable: 1

The system is stable and the stability margins are good.

The bode plot of the loop gain \(L = K*G*H_L\) is shown on figure 18.

bode_plot_loop_gain.png

Figure 18: Bode Plot of the Loop Gain \(L = K G H_L\) (png, pdf)

In order to check the Nominal Performance of the system, we compute the sensibility and the complementary sensibility transfer functions.

S = 1/(K*G*Hl_hinf + 1);
T = K*G*Hl_hinf/(K*G*Hl_hinf + 1);

We then compare their norms with the upper bounds on the performance of the system (figure 19). As expected, we guarantee the Nominal Performance of the system.

verification_NP.png

Figure 19: Bode plot of \(S\) and \(T\) in order to verify the nominal performance of the system (png, pdf)

10 Robust Stability and Robust Performance

In order to verify the Robust stability of the system, we can use the following equivalence: \[ \text{RS} \Leftrightarrow \left| w_I T \right| < 1 \quad \forall \omega \]

This is shown on figure 20.

robust_stability.png

Figure 20: Robust Stability Check: \(|w_I T| < 1, \quad \forall \omega\) (png, pdf)

To check Robust Stability, we can also look at the loop gain of the uncertain system (figure 21) or the Nyquist plot (figure 22).

loop_gain_robustness.png

Figure 21: Loop Gain of the uncertain system (png, pdf)

nyquist_robustness.png

Figure 22: Nyquist plot of the uncertain system (png, pdf)

The Robust Performance is verified by plotting \(|S|\) and \(|T|\) for the uncertain system along side the upper bounds defined for performance. This is shown on figure 23 and we can indeed confirmed that the robust performance property of the system is valid.

robust_performance_result.png

Figure 23: Verification of the Robust Performance (png, pdf)

11 Pre-filter

For now, we have not specified any performance requirements on the input usage due to change of reference. Do limit the input usage due to change of reference, we can use a pre-filter \(K_r\) as shown on figure 1.

If we want a response time of 0.01 second, we can choose a first order low pass filter with a crossover frequency at \(1/0.01 = 100\ \text{Hz}\) as defined below.

Kr = 1/(1+s/2/pi/100);

We then run a simulation for a step of \(1\mu m\) for the system without and with the pre-filter \(K_r\) (figure 24). This confirms that a pre-filter can be used to limit the input usage due to change of reference using this architecture.

t  = linspace(0, 0.02, 1000);

opts = stepDataOptions;
opts.StepAmplitude = 1e-6;

u  = step((K)/(1+G*K*Hl_hinf),      t, opts);
uf = step((Kr*K)/(1+G*K*Hl_hinf),   t, opts);
y  = step((K*G)/(1+G*K*Hl_hinf),    t, opts);
yf = step((Kr*G*K)/(1+G*K*Hl_hinf), t, opts);

u_and_y_with_Kr.png

Figure 24: Input usage and response due to a step change of reference when using a pre-filter \(K_r\) (png, pdf)

12 Controller using classical techniques

A controller is designed using SISOTOOL with a bandwidth of approximately \(20\ \text{Hz}\) and with two integrator.

The obtained controller is shown below.

Kf = 1.1814e12*(s+10.15)*(s+9.036)*(s+53.8)/(s^2*(s+216.1)*(s+1200)*(s+1864));
zpk(Kf)
zpk(Kf)

ans =

  1.1814e12 (s+10.15) (s+9.036) (s+53.8)
  --------------------------------------
     s^2 (s+216.1) (s+1200) (s+1864)

Continuous-time zero/pole/gain model.

The loop gain for both cases are compared on figure 25.

loop_gain_compare.png

Figure 25: Comparison of the Loop Gains (png, pdf)

The Robust Stability of the system is verified using the Nyquist plot on figure 26.

nyquist_plot_sisotool_controller.png

Figure 26: Nyquist Plot of the uncertain system (png, pdf)

The closed loop sensitivity and complementary sensitivity transfer functions are computed. And finally, the Robust Performance of both systems are compared on figure 27.

robust_performance_compare.png

Figure 27: Comparison of the Robust Performance for both controllers (png, pdf)

Author: Thomas Dehaeze

Created: 2019-08-21 mer. 16:03

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