How to improve an MPC (Model Predictive Control) performance?

18 Ansichten (letzte 30 Tage)
David Cho
David Cho am 30 Jan. 2018
Hi, I'd like to regulate an output of a second-order system using MPC. But I always get a result with a huge undershoot. Could anyone let me know how to remove this undershoot? I've changed weight matrices and prediction/control horizons, but still failed to get a good result. Below is the code I've made. Thank you.
clear all; clc;
A=[1 1;0 1];
B=[0.5;1];
C=[1 0];
D=zeros(1,1);
IC=[1;0];
Ts=0.1;
SYS=ss(A,B,C,D,Ts);
MSYS = minreal(SYS);
np=10; % prediction horizon
nc=4; % control horizon
mpcobj=mpc(MSYS,Ts,np,nc);
Q=1.e+3;
R=1.e+0;
mpcobj.Weights.OutputVariables={Q};
mpcobj.Weights.ManipulatedVariables={R};
Tstop=20;
Tf=round(Tstop/Ts);
r=zeros(Tf,1);
options=mpcsimopt(mpcobj);
options.PlantInitialState=IC;
[y,t,u]=sim(mpcobj,Tf,r,options);
figure;
subplot(1,2,1);plot(t,u);xlabel('Time');ylabel('Control');
subplot(1,2,2);plot(t,y);xlabel('Time');ylabel('Output');

Antworten (1)

Arkadiy Turevskiy
Arkadiy Turevskiy am 16 Aug. 2018
The undershoot you are seeing is due to two reasons:
1. Mismatch between plant and controller initial conditions.
2. Controller is tuned in such a way that even with initial conditions matching, it would produce a significant overshoot for a step response.
Unless initial conditions are matched, you will have some overshoot. You can improve controller design to help with issue 2 though.
I am pasting the code below where I did the following:
a. Changed the scaling factor on output variable to make the problem better conditioned numerically. You can determine that scaling needs to be done if you do review(mpcobj) on your controller - you will see the advice to change the scaling factor.
b. I tweaked the weights, including adding a weight on mv.rate
c. I initialized controller IC to match plant IC. You can comment this line out if you want to keep controller IC mismatched to plant IC.
clear all; clc;
%%plant
A=[1 1;0 1];
B=[0.5;1];
C=[1 0];
D=zeros(1,1);
IC=[1;0];
Ts=0.1;
SYS=ss(A,B,C,D,Ts);
% MSYS = minreal(SYS); %does not reduce any states
np=10; % prediction horizon
nc=3; % control horizon %note change to 3
mpcobj=mpc(SYS,Ts,np,nc);
mpcobj.OV(1).ScaleFactor = 100; %note the use of scaling factor - helps with overshoot
%%specify overall adjustment factor applied to weights
% these weights are result of trial and error in the MPC Designer app
beta = 0.26714;
%%specify weights
mpcobj.Weights.MV = 1*beta;
mpcobj.Weights.MVRate = 0.1/beta;
mpcobj.Weights.OV = 100*beta;
mpcobj.Weights.ECR = 1000000;
%%Need to initialize controller state, otherwise can't avoid initial undershoot
xmpc=mpcstate(mpcobj);
xmpc.Plant=IC;
Tstop=20;
Tf=round(Tstop/Ts);
% keep stepoint at 0 for first 10 secs, then step to 1 - to check transient
% response
r=zeros(Tf,1);
r(100:size(r))=r(100:size(r))+1;
%%set pland and controller initial conditions
options=mpcsimopt(mpcobj);
options.PlantInitialState=IC;
options.ControllerInitialState=xmpc;
[y,t,u]=sim(mpcobj,Tf,r,options);
figure;
subplot(1,2,1);plot(t,u);xlabel('Time');ylabel('Control');
subplot(1,2,2);plot(t,y);xlabel('Time');ylabel('Output');

Kategorien

Mehr zu Linear Plant Specification finden Sie in Help Center und File Exchange

Tags

Community Treasure Hunt

Find the treasures in MATLAB Central and discover how the community can help you!

Start Hunting!

Translated by