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v1.0 
Misr University for Science and Technology 
College of Engineering 
Mechatronics Lab 
PROCESS CONTROL MODULE 
PID TUNING AND STABILITY 
(MATLAB Simulation) 
Prof. Farid A. Tolbah 
Eng. Waleed A. El-Badry
v1.0 
1. Objective 
The experiment is aimed to make student acquainted with the preliminary steps to manually tune a PID controller for a plant model by means of MATLAB. 
2. Outcome 
 Writing mathematical models of plants under investigation in Laplace form using MATLAB. 
 Developing the mathematical Laplace representation of Ziegler-Nicholas PID controller in MATLAB. 
 Finding the critical gain (Kc) and the ultimate period (Pu) to calculate PID gains. 
3. Prerequisite 
Student should be familiar with the following terms: 
 Closed loop system. 
 System response. 
 PID controller 
 Ziegler-Nicholas tuning method. 
Also basic understanding of MATLAB syntax is preferred. 
4. The Closed loop system 
The below figure represents the generic closed loop system. 
Figure 1 Closed loop system 
For implementation in this experiment, we are given the following plant model Wp(s): 푊푝(푠)= 1(10푠+1)3= 11000푆3+300푠2+30푠+1 
And the Ziegler-Nicholas PID is formulated as: 푊푐(푠)=퐾푐(1+ 1 푇푖푠 +푇푑푠) 
Controller 
Plant 
Feedback 
FCE 
Set 
Point 
e(t) 
y(t) 
wc 
Current 
Level
v1.0 
Assuming unity feedback, redrawing the block diagram: 
Figure 2 Problem block diagram 
5. Developing MATLAB functions (Plant, Controller and Closed Loop) 
a. Launch MATLAB software. 
b. From the Home tab, select New -> Function. 
c. Write down the generic plant function as shown in the following snippet: 
function [ Wp ] = CreatePlant( num,den ) 
%CreatePlant Creates plant transfer function. 
% The returned value is the system in numerator/denomerator format 
%% Parameters 
% num : Numerator vector (starting from highest order of coefficients) 
% den : Denomerator vector (starting from highest order of coefficients) 
% plant : Plant transfer function 
%% EXAMPLE 
% num=[1]; 
% den=[1 0 1]; 
% sys=CreatePlant(num,den) 
%% Result is 
% 1 
% sys= --------------- 
% S^2+1 
%% Function implementation 
syms s; 
Wp=tf(num,den); 
end 
Snippet 1 CreatePlant function 
d. Save the file. 
e. Close the function file. 
퐾푐(1+ 1 푇푖푠 +푇푑푠) 
1(10푠+1)3 
Set 
Point 
E(S) 
X(S) 
Current 
Level 
Y(S)
v1.0 
f. Repeat steps b-e for creating the following snippet for Ziegler-Nicholas generic function: 
function Wc = ZieglerNicholasPID( Kc,Ti,Td ) 
% ZieglerNicholasPID function to generate the PID controller transfer 
%% Parameters 
% Kc : Critical gain 
% Ti : Reset time (minutes) 
% Td : Derivative time (minutes) 
%% Function implementation 
s=tf('s'); 
Wc=Kc*(1+(1/(Ti*s))+Td*s); 
end 
Snippet 2 Ziger-Nicholas PID implementation 
g. The final function bonds the two functions (plant and controller) to build the closed loop system: 
function sys = CLS( Wp,Wc ) 
%CLS Closed loop system function 
%% Parameters 
% Wp : Plant transfer function 
% Wc : Controller transfer function 
% sys : Closed Loop transfer function with assuming unity feedback. 
%% Function implementation 
CLS=feedback(series(Wp,Wc),1); 
end 
Snippet 3 Closed loop system bonding
v1.0 
6. Open loop system response 
Figure 3 Open loop system 
To plot the open loop response, perform the following steps: 
a. From MATLAB command window, we will call the function CreatePlant to create the transfer function mentioned in shown: 
sys=CreatePlant(1,[1000 300 30 1]); 
step(sys) 
b. From the figure opened, right click on it and select characteristics -> Settling Time, Rise Time and Steady State. Fill in the table: 
Figure 4 Characteristics of Open loop system 
 
Table 1 Characteristics of open loop system 
Rise Time (sec) 
42.2 
Settling Time (sec) 
75.2 
Steady State (sec) 
120 
1(10푠+1)3 
Set 
Point 
Y(s)
v1.0 
7. Finding the critical gain (Kc) via Nyquist plot 
a. To plot the Nyquist of frequency response of the plant, write down the following code: 
Wp=CreatePlant(1,[1000 300 30 1]); 
nyquist(Wp); 
b. Right click on the plot and select characteristics -> Minimum Stability Margins as shown in figure 
Figure 5 Nyquist plot (Open loop) 
c. Write down the gain margin Gm (in dB) and convert it to magnitude. Write down the margin frequency Wc . 
d. Calculate 퐾푐=퐺푚= 8.0011 , and 푃푢= 2휋 휔푐 = 2휋 0.173=36.32 푠푒푐 and consequently 푇푖=
v1.0 
e. Check that Kc is the critical gain by writing down the following MATLAB code: 
t=0:0.01:200; 
Wp=CreatePlant(1,[1000 300 30 1]); 
%Setting Kc=8, Ki=~0 and Kd=0 
Wc=ZieglerNicholasPID(8,100000,0); 
sys=CLS(Wp,Wc); 
%plotting step response from t0=0 to tf=200 sec 
step(sys,t) 
Snippet 4 Plotting the system response at critical gain 
Figure 6 Step response at Kc=8 
8. Calculating P, PI and PID control gains 
After obtaining the critical gain from the previous step, we are able to calculate the P,I and D parameters and perform comparison of each controller type. According to Ziegler Nicholas table: 
Table 2 Ziegler Nicholas Tuning Chart Controller Type Kp Ti (sec) Td (sec) P 
0.5*Kc = 0.5*8=4 
100000 
0 PI 
0.45*Kc = 0.45*8=3.6 
0.83*Pu=0.83*36.32=30.1 
0 PID 
0.59* Kc = 0.59*8=4.7 
0.5*Pu=0.5*36.32=18.2 
0.12*Pu =0.12*36.32=4.4
v1.0 
Plot the step response of each controller over the plant by writing the following code: 
Wp=CreatePlant(1,[1000 300 30 1]); 
Wcp=ZieglerNicholasPID(4,100000,0); 
Wcpi=ZieglerNicholasPID(3.6,30.1,0); 
Wcpid=ZieglerNicholasPID(4.7,18.2,4.4); 
t=0:0.01:500; 
sys=CLS(Wp,Wcp); 
step(sys,t) 
hold on 
sys=CLS(Wp,Wcpi); 
step(sys,t) 
sys=CLS(Wp,Wcpid); 
step(sys,t) 
legend('P','PI','PID') 
Figure 7 step response of P, PI and PID controller

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PID Tuning using Ziegler Nicholas - MATLAB Approach

  • 1. v1.0 Misr University for Science and Technology College of Engineering Mechatronics Lab PROCESS CONTROL MODULE PID TUNING AND STABILITY (MATLAB Simulation) Prof. Farid A. Tolbah Eng. Waleed A. El-Badry
  • 2. v1.0 1. Objective The experiment is aimed to make student acquainted with the preliminary steps to manually tune a PID controller for a plant model by means of MATLAB. 2. Outcome  Writing mathematical models of plants under investigation in Laplace form using MATLAB.  Developing the mathematical Laplace representation of Ziegler-Nicholas PID controller in MATLAB.  Finding the critical gain (Kc) and the ultimate period (Pu) to calculate PID gains. 3. Prerequisite Student should be familiar with the following terms:  Closed loop system.  System response.  PID controller  Ziegler-Nicholas tuning method. Also basic understanding of MATLAB syntax is preferred. 4. The Closed loop system The below figure represents the generic closed loop system. Figure 1 Closed loop system For implementation in this experiment, we are given the following plant model Wp(s): 푊푝(푠)= 1(10푠+1)3= 11000푆3+300푠2+30푠+1 And the Ziegler-Nicholas PID is formulated as: 푊푐(푠)=퐾푐(1+ 1 푇푖푠 +푇푑푠) Controller Plant Feedback FCE Set Point e(t) y(t) wc Current Level
  • 3. v1.0 Assuming unity feedback, redrawing the block diagram: Figure 2 Problem block diagram 5. Developing MATLAB functions (Plant, Controller and Closed Loop) a. Launch MATLAB software. b. From the Home tab, select New -> Function. c. Write down the generic plant function as shown in the following snippet: function [ Wp ] = CreatePlant( num,den ) %CreatePlant Creates plant transfer function. % The returned value is the system in numerator/denomerator format %% Parameters % num : Numerator vector (starting from highest order of coefficients) % den : Denomerator vector (starting from highest order of coefficients) % plant : Plant transfer function %% EXAMPLE % num=[1]; % den=[1 0 1]; % sys=CreatePlant(num,den) %% Result is % 1 % sys= --------------- % S^2+1 %% Function implementation syms s; Wp=tf(num,den); end Snippet 1 CreatePlant function d. Save the file. e. Close the function file. 퐾푐(1+ 1 푇푖푠 +푇푑푠) 1(10푠+1)3 Set Point E(S) X(S) Current Level Y(S)
  • 4. v1.0 f. Repeat steps b-e for creating the following snippet for Ziegler-Nicholas generic function: function Wc = ZieglerNicholasPID( Kc,Ti,Td ) % ZieglerNicholasPID function to generate the PID controller transfer %% Parameters % Kc : Critical gain % Ti : Reset time (minutes) % Td : Derivative time (minutes) %% Function implementation s=tf('s'); Wc=Kc*(1+(1/(Ti*s))+Td*s); end Snippet 2 Ziger-Nicholas PID implementation g. The final function bonds the two functions (plant and controller) to build the closed loop system: function sys = CLS( Wp,Wc ) %CLS Closed loop system function %% Parameters % Wp : Plant transfer function % Wc : Controller transfer function % sys : Closed Loop transfer function with assuming unity feedback. %% Function implementation CLS=feedback(series(Wp,Wc),1); end Snippet 3 Closed loop system bonding
  • 5. v1.0 6. Open loop system response Figure 3 Open loop system To plot the open loop response, perform the following steps: a. From MATLAB command window, we will call the function CreatePlant to create the transfer function mentioned in shown: sys=CreatePlant(1,[1000 300 30 1]); step(sys) b. From the figure opened, right click on it and select characteristics -> Settling Time, Rise Time and Steady State. Fill in the table: Figure 4 Characteristics of Open loop system Table 1 Characteristics of open loop system Rise Time (sec) 42.2 Settling Time (sec) 75.2 Steady State (sec) 120 1(10푠+1)3 Set Point Y(s)
  • 6. v1.0 7. Finding the critical gain (Kc) via Nyquist plot a. To plot the Nyquist of frequency response of the plant, write down the following code: Wp=CreatePlant(1,[1000 300 30 1]); nyquist(Wp); b. Right click on the plot and select characteristics -> Minimum Stability Margins as shown in figure Figure 5 Nyquist plot (Open loop) c. Write down the gain margin Gm (in dB) and convert it to magnitude. Write down the margin frequency Wc . d. Calculate 퐾푐=퐺푚= 8.0011 , and 푃푢= 2휋 휔푐 = 2휋 0.173=36.32 푠푒푐 and consequently 푇푖=
  • 7. v1.0 e. Check that Kc is the critical gain by writing down the following MATLAB code: t=0:0.01:200; Wp=CreatePlant(1,[1000 300 30 1]); %Setting Kc=8, Ki=~0 and Kd=0 Wc=ZieglerNicholasPID(8,100000,0); sys=CLS(Wp,Wc); %plotting step response from t0=0 to tf=200 sec step(sys,t) Snippet 4 Plotting the system response at critical gain Figure 6 Step response at Kc=8 8. Calculating P, PI and PID control gains After obtaining the critical gain from the previous step, we are able to calculate the P,I and D parameters and perform comparison of each controller type. According to Ziegler Nicholas table: Table 2 Ziegler Nicholas Tuning Chart Controller Type Kp Ti (sec) Td (sec) P 0.5*Kc = 0.5*8=4 100000 0 PI 0.45*Kc = 0.45*8=3.6 0.83*Pu=0.83*36.32=30.1 0 PID 0.59* Kc = 0.59*8=4.7 0.5*Pu=0.5*36.32=18.2 0.12*Pu =0.12*36.32=4.4
  • 8. v1.0 Plot the step response of each controller over the plant by writing the following code: Wp=CreatePlant(1,[1000 300 30 1]); Wcp=ZieglerNicholasPID(4,100000,0); Wcpi=ZieglerNicholasPID(3.6,30.1,0); Wcpid=ZieglerNicholasPID(4.7,18.2,4.4); t=0:0.01:500; sys=CLS(Wp,Wcp); step(sys,t) hold on sys=CLS(Wp,Wcpi); step(sys,t) sys=CLS(Wp,Wcpid); step(sys,t) legend('P','PI','PID') Figure 7 step response of P, PI and PID controller