mpcmove

Compute optimal control action

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Syntax

mv = mpcmove(MPCobj,x,ym,r,v)
[mv,info] = mpcmove(MPCobj,x,ym,r,v)
[___] = mpcmove(___,options)

Description

mv = mpcmove(MPCobj,x,ym,r,v) computes the optimal manipulated variable moves, u(k), at the current time. u(k) is calculated given the current estimated extended state, x(k), the measured plant outputs, ym(k), the output references, r(k), and the measured disturbances, v(k), at the current time k. Call mpcmove repeatedly to simulate closed-loop model predictive control.

[mv,info] = mpcmove(MPCobj,x,ym,r,v) returns additional information regarding the model predictive controller in the second output argument info.

[___] = mpcmove(___,options) overrides default constraints and weights settings in MPCobj with the values specified by Options, an mpcmoveopt object. Use Options to provide run-time adjustment of constraints and weights during the closed-loop simulation.

Input Arguments

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Model predictive controller, specified as an MPC controller object. To create an MPC controller, use mpc.

Current controller state, specified as an mpcstate object.

Before you begin a simulation with mpcmove, initialize the controller state using x = mpcstate(MPCobj). Then, modify the default properties of x as appropriate. mpcmove modifies the value of x to reflect the current state of the controller.

If you are using default state estimation, mpcmove expects x to represent x[n|n-1]. The mpcmove command updates the state values in the previous control interval with that information. Therefore, you should not programmatically update x at all. The default state estimator employs a steady-state Kalman filter.

If you are using custom state estimation, mpcmove expects x to represent x[n|n]. Therefore, prior to each mpcmove command, you must set x.Plant, x.Disturbance, and x.Noise to the best estimates of these states (using the latest measurements) at the current control interval.

Current measured output values at time k, specified as a column vector of length Nym, where Nym is the number of measured outputs.

If you are using custom state estimation, set ym = [].

Plant output reference values, specified as a p-by-Ny array, where p is the prediction horizon of MPCobj and Ny is the number of outputs. Row r(i,:) defines the reference values at step i of the prediction horizon.

r must contain at least one row. If r contains fewer than p rows, mpcmove duplicates the last row to fill the p-by-Ny array. If you supply exactly one row, therefore, a constant reference applies for the entire prediction horizon.

To implement reference previewing, which can improve tracking when a reference varies in a predictable manner, r must contain the anticipated variations, ideally for p steps.

Current and anticipated measured disturbances, specified as a (p+1)-by-Nmd array, where p is the prediction horizon of MPCobj and Nmd is the number of measured disturbances. The first row of v specifies the current measured disturbance values. Row v(i+1,:) defines the anticipated disturbance values at step i of the prediction horizon.

Modeling of measured disturbances provides feedforward control action. If your plant model does not include measured disturbances, use v = [].

If your model includes measured disturbances, v must contain at least one row. If v contains fewer than p+1 rows, mpcmove duplicates the last row to fill the (p+1)-by-Nmd array. If you supply exactly one row, a constant measured disturbance applies for the entire prediction horizon.

To implement disturbance previewing, which can improve tracking when a disturbance varies in a predictable manner, v must contain the anticipated variations, ideally for p steps.

Run-time options, specified as an mpcmoveopt object. Use options to override selected properties of MPCobj during simulation. These options apply to the current mpcmove time instant only. Using options yields the same result as redefining or modifying MPCobj before each call to mpcmove, but involves considerably less overhead. Using options is equivalent to using an MPC Controller Simulink® block in combination with optional input signals that modify controller settings, such as MV and OV constraints.

Output Arguments

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Optimal manipulated variable moves, returned as a column vector of length Nmv, where Nmv is the number of manipulated variables.

If the controller detects an infeasible optimization problem or encounters numerical difficulties in solving an ill-conditioned optimization problem, mv remains at its most recent successful solution, x.LastMove.

Otherwise, if the optimization problem is feasible and the solver reaches the specified maximum number of iterations without finding an optimal solution, mv:

  • Remains at its most recent successful solution if the Optimizer.UseSuboptimalSolution property of the controller is false.

  • Is the suboptimal solution reached after the final iteration if the Optimizer.UseSuboptimalSolution property of the controller is true. For more information, see Suboptimal QP Solution.

Solution details, returned as a structure with the following fields.

Predicted optimal manipulated variable adjustments (moves), returned as a (p+1)-by-Nmv array, where p is the prediction horizon and Nmv is the number of manipulated variables.

Uopt(i,:) contains the calculated optimal values at time k+i-1, for i = 1,...,p, where k is the current time. The first row of Info.Uopt contains the same manipulated variable values as output argument mv. Since the controller does not calculate optimal control moves at time k+p, Uopt(p+1,:) is equal to Uopt(p,:).

Optimal output variable sequence, returned as a (p+1)-by-Ny array, where p is the prediction horizon and Ny is the number of outputs.

The first row of Info.Yopt contains the calculated outputs at time k based on the estimated states and measured disturbances; it is not the measured output at time k. Yopt(i,:) contains the predicted output values at time k+i-1, for i = 1,...,p+1.

Yopt(i,:) contains the calculated output values at time k+i-1, for i = 2,...,p+1, where k is the current time. Yopt(1,:) is computed based on the estimated states and measured disturbances.

Optimal prediction model state sequence, returned as a (p+1)-by-Nx array, where p is the prediction horizon and Nx is the number of states in the plant and unmeasured disturbance models (states from noise models are not included).

Xopt(i,:) contains the calculated state values at time k+i-1, for i = 2,...,p+1, where k is the current time. Xopt(1,:) is the same as the current states state values.

Time intervals, returned as a column vector of length p+1. Topt(1) = 0, representing the current time. Subsequent time steps Topt(i) are given by Ts*(i-1), where Ts = MPCobj.Ts is the controller sample time.

Use Topt when plotting Uopt, Xopt, or Yopt sequences.

Slack variable, ε, used in constraint softening, returned as 0 or a positive scalar value.

  • ε = 0 — All constraints were satisfied for the entire prediction horizon.

  • ε > 0 — At least one soft constraint is violated. When more than one constraint is violated, ε represents the worst-case soft constraint violation (scaled by your ECR values for each constraint).

See Optimization Problem for more information.

Number of solver iterations, returned as one of the following:

  • Positive integer — Number of iterations needed to solve the optimization problem that determines the optimal sequences.

  • 0 — Optimization problem could not be solved in the specified maximum number of iterations.

  • –1 — Optimization problem was infeasible. An optimization problem is infeasible if no solution can satisfy all the hard constraints.

  • –2 — Numerical error occurred when solving the optimization problem.

Optimization solution status, returned as one of the following:

  • 'feasible' — Optimal solution was obtained (Iterations > 0)

  • 'infeasible' — Solver detected a problem with no feasible solution (Iterations = –1) or a numerical error occurred (Iterations = –2)

  • 'unreliable' — Solver failed to converge (Iterations = 0). In this case, if MPCobj.Optimizer.UseSuboptimalSolution is false, u freezes at the most recent successful solution. Otherwise, it uses the suboptimal solution found during the last solver iteration.

Objective function cost, returned as a nonnegative scalar value. The cost quantifies the degree to which the controller has achieved its objectives. For more information, see Optimization Problem.

The cost value is only meaningful when QPCode = 'feasible', or when QPCode = 'feasible' and MPCobj.Optimizer.UseSuboptimalSolution is true.

Examples

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Open Live Script

Perform closed-loop simulation of a plant with one MV and one measured OV.

Define a plant model and create a model predictive controller with MV constraints.

ts = 2;
Plant = ss(0.8,0.5,0.25,0,ts);
MPCobj = mpc(Plant);
-->The "PredictionHorizon" property of "mpc" object is empty. Trying PredictionHorizon = 10.
-->The "ControlHorizon" property of the "mpc" object is empty. Assuming 2.
-->The "Weights.ManipulatedVariables" property of "mpc" object is empty. Assuming default 0.00000.
-->The "Weights.ManipulatedVariablesRate" property of "mpc" object is empty. Assuming default 0.10000.
-->The "Weights.OutputVariables" property of "mpc" object is empty. Assuming default 1.00000.

MPCobj.MV(1).Min = -2;
MPCobj.MV(1).Max = 2;

Initialize an mpcstate object for simulation. Use the default state properties.

x = mpcstate(MPCobj);
-->Assuming output disturbance added to measured output channel #1 is integrated white noise.
-->The "Model.Noise" property of the "mpc" object is empty. Assuming white noise on each measured output channel.

Set the reference signal. There is no measured disturbance.

r = 1;

Simulate the closed-loop response by calling mpcmove iteratively.

t = [0:ts:40];
N = length(t);
y = zeros(N,1); 
u = zeros(N,1); 
for i = 1:N
    % simulated plant and predictive model are identical
    y(i) = 0.25*x.Plant;
    u(i) = mpcmove(MPCobj,x,y(i),r);
end

y and u store the OV and MV values.

Analyze the result.

[ts,us] = stairs(t,u);
plot(ts,us,'r-',t,y,'b--')
legend('MV','OV')

Modify the MV upper bound as the simulation proceeds using an mpcmoveopt object.

MPCopt = mpcmoveopt;
MPCopt.MVMin = -2;
MPCopt.MVMax = 2;

Simulate the closed-loop response and introduce the real-time upper limit change at eight seconds (the fifth iteration step).

x = mpcstate(MPCobj);
y = zeros(N,1);
u = zeros(N,1);
for i = 1:N
    % simulated plant and predictive model are identical
    y(i) = 0.25*x.Plant;
    if i == 5
    	MPCopt.MVMax = 1;
    end
    u(i) = mpcmove(MPCobj,x,y(i),r,[],MPCopt);
end

Analyze the result.

[ts,us] = stairs(t,u);
plot(ts,us,'r-',t,y,'b--')
legend('MV','OV')

Open Live Script

Define a plant model.

ts = 2;
Plant = ss(0.8,0.5,0.25,0,ts);

Create a model predictive controller with constraints on both the manipulated variable and the rate of change of the manipulated variable. The prediction horizon is 10 intervals, and the control horizon is blocked.

MPCobj = mpc(Plant,ts,10,[2 3 5]);
-->The "Weights.ManipulatedVariables" property of "mpc" object is empty. Assuming default 0.00000.
-->The "Weights.ManipulatedVariablesRate" property of "mpc" object is empty. Assuming default 0.10000.
-->The "Weights.OutputVariables" property of "mpc" object is empty. Assuming default 1.00000.

MPCobj.MV(1).Min = -2;
MPCobj.MV(1).Max = 2;
MPCobj.MV(1).RateMin = -1;
MPCobj.MV(1).RateMax = 1;

Initialize an mpcstate object for simulation from a particular state.

x = mpcstate(MPCobj);
-->Assuming output disturbance added to measured output channel #1 is integrated white noise.
-->The "Model.Noise" property of the "mpc" object is empty. Assuming white noise on each measured output channel.

x.Plant = 2.8;
x.LastMove = 0.85;

Compute the optimal control at current time.

y = 0.25*x.Plant;
r = 1;
[u,Info] = mpcmove(MPCobj,x,y,r);

Analyze the predicted optimal sequences.

[ts,us] = stairs(Info.Topt,Info.Uopt);
plot(ts,us,'r-',Info.Topt,Info.Yopt,'b--')
legend('MV','OV')

plot ignores Info.Uopt(end) as it is NaN.

Examine the optimal cost.

Info.Cost
ans = 0.0793

Tips

  • mpcmove updates x.

  • If ym, r or v is specified as [], mpcmove uses the appropriate MPCobj.Model.Nominal value instead.

  • To view the predicted optimal behavior for the entire prediction horizon, plot the appropriate sequences provided in Info.

  • To determine the optimization status, check Info.Iterations and Info.QPCode.

Alternatives

  • Use sim for plant mismatch and noise simulation when not using run-time constraints or weight changes.

  • Use the MPC Designer app to interactively design and simulate model predictive controllers.

  • Use the MPC Controller block in Simulink and for code generation.

  • Use mpcmoveCodeGeneration for code generation.

See Also

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Topics

Introduced before R2006a

Model Predictive Control Toolbox Documentation

Support