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International Journal of Power Electronics and Drive System (IJPEDS)
Vol. 10, No. 4, December 2019, pp. 1734~1741
ISSN: 2088-8694, DOI: 10.11591/ijpeds.v10.i4.pp1734-1741  1734
Journal homepage: http://iaescore.com/journals/index.php/IJPEDS
Determination of all stability region of unstable fractional order
system in case of bearing system
Phu Tran Tin1
, Nguyen Quang Dung2
, Minh Tran3
, Van-Duc Phan4
, Hoang-Nam Nguyen5
, Tran
Thanh Trang6
1Wireless Communications Research Group, Faculty of Electrical and Electronics Engineering,
Ton Duc Thang University, Ho Chi Minh City, Vietnam
2Faculty of Electrical and Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam
3Optoelectronics Research Group, Faculty of Electrical and Electronics Engineering, Ton Duc Thang University,
Ho Chi Minh City, Vietnam
4Center of Excellence for Automation and Precision Mechanical Engineering, Nguyen Tat Thanh University,
Ho Chi Minh City, Vietnam
5Modeling Evolutionary Algorithms Simulation and Artificial Intelligence, Faculty of Electrical & Electronics
Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam
6Faculty of Electrical and Electronics Engineering, Ho Chi Minh City University of Food Industry, 140 Le Trong Tan,
Ho Chi Minh City, Vietnam.
Article Info ABSTRACT
Article history:
Received Dec 18, 2018
Revised Mar 1, 2019
Accepted May 28, 2019
In this paper, we propose and investigate the optimal tuning PID
controller of unstable fractional order system by desired transient
characteristics using the real interpolation method (RIM). The
research shows that the main advantages of this method are drawn
as the followings: 1) Carrying out an investigation of the stable
region of coefficients of a PID controller using D-decomposition
method; 2) Applying the method to investigate an unstable fractional
order system.
Keywords:
Control system
PID
RIM
Unstable fractional order
system Copyright © 2019 Institute of Advanced Engineering and Science.
All rights reserved.
Corresponding Author:
Van-Duc Phan
Center of Excellence for Automation and Precision Mechanical Engineering,
Nguyen Tat Thanh University, Ho Chi Minh City, Vietnam
Email: pvduc@ntt.edu.vn
1. INTRODUCTION
Due to the individual merits such as no contact, no wear, no lubrication and adjustable dynamics,
magnetic bearings (MBs) are being widely applied to a variety of industrial products, especially the high-
speed rotating machinery and precise positioning systems [1-3]. Considering the inherent nonlinearity and
open-loop instability of MBs, the accurate modeling and control are two essential aspects of achieving high-
performance requirements. Nowadays, PID controllers have received considerable attention in the last years
both from an academic and industrial point of view [1-5]. In fact, in principle, they provide more flexibility
in the controller design, concerning the standard PID controllers, because they have five parameters to select.
However, this also implies that the tuning of the controller can be much more complicated. They have been
successfully applied in practical applications such as motion control of manipulators and chaos control of
electrical circuits. In these applications, it has been verified that PID controllers can improve the performance
of traditional control system adopting integer order PID controllers. The most important advantage of the PID
controllers is that they can afford broader possibilities offered by their new fractional order dynamics [4-7].
Int J Pow Elec & Dri Syst ISSN: 2088-8694 
Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan)
1735
However, this also indicates that the tuning strategies of PID controllers are much more complicated. In the
researches on the PID controllers, tuning of controller parameters has become a significant issue.
In general, the tuning methods for PID controllers are classified into analytical, numerical, and rule-
based ones. In [6-7] the controller parameters have been analytically derived by solving nonlinear equations
fulfilling the gain/phase crossover frequency and phase/gain margin specifications. The robustness to loop
gain variations specification proposed in [8] has also been widely used to design PID and proportional–
integral (PI) controllers. The merits of the analytical method are apparent; however, it is available only when
the equations are few in number and simple. Therefore, it is challenging to obtain a complete PID controller
for the MB system by solving five complicated nonlinear equations. As for the rule-based method, it can
easily calculate the controller parameters based on empirical tuning rules, which can be observed in [9-21]. In
this paper, we propose and investigate the optimal tuning PID controller of unstable fractional order system
by desired transient characteristics using the real interpolation method (RIM). The main advantages of this
method are drawn as the followings:
1) Carrying out an investigation of the stable region of coefficients of a PID controller using D-
decomposition method.
2) Applying the method to investigate an unstable fractional order system.
The rest of this paper is organized as follows. In Section 2 the problem is formulated. Numerical
results and discussions are described in Section 3. Conclusions are drawn in Section 4.
2. PROBLEM FORMULATION
In this section, Figure 1 illustrates the control system with the negative unity feedback. The
mathematical description of this model is presented.
Figure 1. Control system with negative unity feedback
The transfer function of the PID controller can be formulated as
K
(s) K K
i
p d
C s
s
   (1)
The transfer function of the plant (in the fractional form) is calculated as
1 0
1
1 0
1
1 1 0
1 1 0
B (s)
G(s)
( )
n n
m m
G n n
G m m
b s b s b s b s
A s a s a s a s a s
  

  





   
 
   


(2)
where 𝑚, 𝑛 ∈ 𝑁, 𝑎𝑛𝑑 𝑎 , … , 𝑎 , 𝑏 , … , 𝑏 , 𝛼 𝛼 ⋯ 𝛼 𝛼 0, 𝛽 𝛽 ⋯ 𝛽 𝛽
0 are arbitrary real numbers 𝑎 0, 𝑏 0.
The transfer function of PID controller (1) can be rewritten in the rational form as the following
2
K K K
( )
(s)
( )
d p i
C
C
s s
B s
C
A s s
 
  (3)
The characteristic equation in this analysis can be expressed as
W( ) 1 (s)G(s)
s C
  (4)
Characteristic polynomial is formulated as
 ISSN: 2088-8694
Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741
1736
 
2
P( ) ( ) K K K B ( )
G d p i G
s sA s s s s
    (5)
A gain-phase margin tester (GPMT) can be thought of as a “virtual compensator”, provides
information for plotting the boundaries of constant gain margin and phase margin in a parameter plane [14].
The frequency independent GPMT is given as in [15]:
(M, ) Me .
j
t
G 
 
 (6)
For a given IOPID controller parameters K , K , K
p i d
the closed-loop system is said to be bounded-
input bounded-output (BIBO) stable if the quasi-polynomial P(s, K , K , K )
p i d
has no roots in the closed right-
half of the s-plane (RHP). The stability domain S in the parameter space P with K , K , K
p i d
being
coordinates is the region that for K , K , K
p i d S
 the roots of quasi-polynomial P(s, K , K , K )
p i d
all lie in
open left-half of the s-plane (LHP). The boundaries of the stability domain S which are described by real root
boundary (RRB), infinite root boundary (IRB) and complex root boundary (CRB) can be determined by the
D-decomposition method [15], [16] . These boundaries are defined by the equations P(0,K) 0
 , P( ,K) 0
 
and P( j ,K) 0

  for (0, )
  , respectively, where P(s,K) is the characteristic function of the closed-
loop system and K the vector of controller parameters.
2.1. Determining RRB
In applying the descriptions of stability boundaries of the stability domain S to the FOCE in (1), the
RRB turns out to be simply a straight line given by
P(0, K , K , K ) 0 0,
p i d i
K
   (7)
for 0
1
s
 in the transfer function of the plant in (2).
2.2. Determining IRB
The calculating of the IRB faces with more technical difficulties due to the fractional component.
FOCE possesses an infinite number of roots, which cannot be calculated analytically in the general case.
However, the asymptotic location of roots far from the origin is well known [17], which may lead to IRB.
The objective of this section is to determine the stabilizing region in 𝐾 , 𝐾 plane with given 𝐾 , and values
for which the following complex polynomial is Hurwitz:
 
2
D( ) ( ) ( ) K K K M(s)B ( )
G d p i G
s sL s A s s s s
    (8)
where L(s) and M(s) are given complex fractional order polynomials. When 𝐿 𝑠 𝑀 𝑠 1, the
stabilization of Eq. (8) reduces to the standard IOPID stabilization.
From (8), we have D( ) 0
  . Suppose when s   ,        
/ t
G G
L s A s M s s
B s c

   
    where t
and c are real and complex numbers respectively. We have [16]:
(a) If 1
t  , then the boundary does not exist.
(b) If 1
t  and c is not real, then the boundary does not exist.
(c) If 1
t  and c is real, then
 
   
  
 
2
lim lim1 1 0
p i d
d
s s
G G
N s K s K K s
D s
K c
sL s A s sA s
 
 
     (9)
1
d
K
c
  (10)
The RRB and IRB lines can be obtained from (7) and (10), respectively.
2.3. Determining CRB 
Int J Pow Elec & Dri Syst ISSN: 2088-8694 
Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan)
1737
To construct the CRB, we substitute s j
 into (5) to obtain
P(j ) (j ) (j ) (j )B (j ) 0
C G C G
A A B
    
   (11)
Using D-decomposition to find stability [15]. In the s plane
( )
2
cos( ) jsin( )
2 2
j
j e


  
 
   ,
where  is a real number. The formula (6) can be expressed into a formula with the separate real and
imaginary components
2
P(j ) (K K )R ( ) I ( ) K R ( ) R ( ) 0
i d BG AG p BG AG
j
       
   
     
    , (12)
where RBG , RAG , IAG are the real component of B (j )
G  , the real and imaginary components of
(j )
G
A  , respectively.
Finally, by setting the real and imaginary parts equalized zero the formula (12) leads to the
detail form:
2
R ( ) K R ( ) 0
(K K )R ( ) I ( ) 0
AG p BG
i d BG AG
 
   
 



  


(13)
The solution in the (Kp, Ki) plane
This is a three-dimensional system in terms of the controller parameters K , K , K
p i d . In order to deal
with two unknowns K , K
p i , the value of Kd will be fixed to find the stability region in the (K , K )
p i plane.
Equation (11) rewrite in terms of two unknowns K , K
p i .
2
K R ( ) / R ( )
K ( ) / R ( ) K
p AG BG
i AG BG d
I
 
   
 



 


(14)
The above two equations trace out a curve in the (K , K )
p i -plane representing the CRB, for fixed
Kd , as  run from 0 to  .
The solution in the (Kp, Kd) plane
Next, to find the stability region in the (Kp, Kd) plane, the value of Ki will be fixed. Then formula
(13) can be rewritten as:
2
K R ( ) / R ( )
K K I ( ) / R ( ) /
p AG BG
d i AG BG
 
   
 



 
 
  

(15)
The above two equations trace out a curve in the (K , K )
p d -plane representing the CRB, for fixed
Ki , as  run from 0 to  .
The solution in the (Ki, Kd) plane
Next, to find the stability region in the (Ki, Kd) plane, the value of Kd will be fixed. Then formula
(13) can be rewritten as:
2
K R ( ) / R ( )
K K I ( ) / R ( ) /
p AG BG
d i AG BG
 
   
 



 
 
  

(16)
The above two equations trace out a curve in the (K , K )
i d -plane representing the CRB, for fixed
Kp , as  run from 0 to  .
3. NUMERICAL SAMPLE AND DISCUSSION
Given fractional order transfer function of an unstable bearing system [18] [19],
 ISSN: 2088-8694
Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741
1738
2.76 1.81 0.82
6438.
G(s)
330.04 84268.85 15869154.14
s s s

  
(17)
Investigation of the stability region of the unstable fractional order transfer function of the bearing system
(17) is carried out in the following parts.
3.1. Determining RRB
It is important to determine the stability region of the PID controller, tuned for the system (17). The
RRB can be determined by (7) as the bellow
0.
i
K  (18)
3.2. Determining IRB
The IRB can be determined according to (9)
 
 
 
2.76 1.81 0
2
.82
330.04
643.8
lim lim1 ) 1
( 84268.85 15869154.14)
p i d
s s s
K s K K s
s
sD s s s s

 
 

 
 

(19)
Not exist the IRB.
Figure 2. The CRB graph in the K , K plane and K 10.
3.3. Determining CRB 
The CRB can be determined by three conditions (13), (14) and (15). Figure 2 shows the stability
region of the transfer function (17). The CRB in the (K_p,K_i) plane when K_d=10 is shown in the Figure 2.
The cross-line area is a feasible region for the coefficients of the PID controller. The cross-line region
demonstrates stability region of K_p,K_i where K_d=10. Obviously, the stability region of PID controller’s
coefficients lie in the first quarter of the coordinate [22-25].
Furthermore, Figure 3 shows a more feasible area with five values of 𝐾 .
Kp
Ki
Ki
Kp
Int J Pow Elec & Dri Syst ISSN: 2088-8694 
Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan)
1739
Figure 3. The CRB graphs in the K , K plane with 5 values of coefficients K .
Figure 3 shows that by increasing the value of the coefficient 𝐾 , the feasible region is expanded.
Figure 4. The CRB of the PID coefficients
In Figure 4. The distribution of 𝐾 , 𝐾 , 𝐾 in the 3-D system is represented. In more details, we can
investigate the stability region of the PID controller’s coefficient separately in the 2-D coordinate plane. In
the Figure 4.
Figure 5. The CRB in the K , K plane
Figure 5 illustrates the stability region of 𝐾 and 𝐾 . Obviously, the stability region is covered the first
and fourth quarters of the coordinate system. From the Figure 5, there is a significance that the coefficient
𝐾 2465. Furthermore, The Figure 6 show the stability region in the 𝐾 , 𝐾 plane. The values of the
coefficient 𝐾 , 𝐾 are located in the first and fourth quarters, and of course 𝐾 2456.
Figure 6. The CRB in the K , K plane
 ISSN: 2088-8694
Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741
1740
The CRB in the K , K plane shows that the distribution of 𝐾 and 𝐾
Figure 7. The CRB in the K , K plane
The results simply lead to the conclusion
2465
0
p
i
K
K







(20)
Three parameters , ,
p i d
K K K of the PID controller are determined in four figure 4-7 [22-25].
4. CONCLUSION
In this paper, we propose and investigate optimal tuning PID controller of unstable fractional order
system by desired transient characteristics using the real interpolation method (RIM). The research shows
that the main advantages of this method are drawn as the followings: 1) Carrying out an investigation of the
stable region of coefficients of a PID controller using D-decomposition method; 2) Applying the method to
investigate an unstable fractional order system.
ACKNOWLEDGEMENTS
This research was supported by National Key Laboratory of Digital Control and System Engineering
(DCSELAB), HCMUT, VNU-HCM, Vietnam.
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Determination of all stability region of unstable fractional order system in case of bearing system

  • 1. International Journal of Power Electronics and Drive System (IJPEDS) Vol. 10, No. 4, December 2019, pp. 1734~1741 ISSN: 2088-8694, DOI: 10.11591/ijpeds.v10.i4.pp1734-1741  1734 Journal homepage: http://iaescore.com/journals/index.php/IJPEDS Determination of all stability region of unstable fractional order system in case of bearing system Phu Tran Tin1 , Nguyen Quang Dung2 , Minh Tran3 , Van-Duc Phan4 , Hoang-Nam Nguyen5 , Tran Thanh Trang6 1Wireless Communications Research Group, Faculty of Electrical and Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam 2Faculty of Electrical and Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam 3Optoelectronics Research Group, Faculty of Electrical and Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam 4Center of Excellence for Automation and Precision Mechanical Engineering, Nguyen Tat Thanh University, Ho Chi Minh City, Vietnam 5Modeling Evolutionary Algorithms Simulation and Artificial Intelligence, Faculty of Electrical & Electronics Engineering, Ton Duc Thang University, Ho Chi Minh City, Vietnam 6Faculty of Electrical and Electronics Engineering, Ho Chi Minh City University of Food Industry, 140 Le Trong Tan, Ho Chi Minh City, Vietnam. Article Info ABSTRACT Article history: Received Dec 18, 2018 Revised Mar 1, 2019 Accepted May 28, 2019 In this paper, we propose and investigate the optimal tuning PID controller of unstable fractional order system by desired transient characteristics using the real interpolation method (RIM). The research shows that the main advantages of this method are drawn as the followings: 1) Carrying out an investigation of the stable region of coefficients of a PID controller using D-decomposition method; 2) Applying the method to investigate an unstable fractional order system. Keywords: Control system PID RIM Unstable fractional order system Copyright © 2019 Institute of Advanced Engineering and Science. All rights reserved. Corresponding Author: Van-Duc Phan Center of Excellence for Automation and Precision Mechanical Engineering, Nguyen Tat Thanh University, Ho Chi Minh City, Vietnam Email: pvduc@ntt.edu.vn 1. INTRODUCTION Due to the individual merits such as no contact, no wear, no lubrication and adjustable dynamics, magnetic bearings (MBs) are being widely applied to a variety of industrial products, especially the high- speed rotating machinery and precise positioning systems [1-3]. Considering the inherent nonlinearity and open-loop instability of MBs, the accurate modeling and control are two essential aspects of achieving high- performance requirements. Nowadays, PID controllers have received considerable attention in the last years both from an academic and industrial point of view [1-5]. In fact, in principle, they provide more flexibility in the controller design, concerning the standard PID controllers, because they have five parameters to select. However, this also implies that the tuning of the controller can be much more complicated. They have been successfully applied in practical applications such as motion control of manipulators and chaos control of electrical circuits. In these applications, it has been verified that PID controllers can improve the performance of traditional control system adopting integer order PID controllers. The most important advantage of the PID controllers is that they can afford broader possibilities offered by their new fractional order dynamics [4-7].
  • 2. Int J Pow Elec & Dri Syst ISSN: 2088-8694  Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan) 1735 However, this also indicates that the tuning strategies of PID controllers are much more complicated. In the researches on the PID controllers, tuning of controller parameters has become a significant issue. In general, the tuning methods for PID controllers are classified into analytical, numerical, and rule- based ones. In [6-7] the controller parameters have been analytically derived by solving nonlinear equations fulfilling the gain/phase crossover frequency and phase/gain margin specifications. The robustness to loop gain variations specification proposed in [8] has also been widely used to design PID and proportional– integral (PI) controllers. The merits of the analytical method are apparent; however, it is available only when the equations are few in number and simple. Therefore, it is challenging to obtain a complete PID controller for the MB system by solving five complicated nonlinear equations. As for the rule-based method, it can easily calculate the controller parameters based on empirical tuning rules, which can be observed in [9-21]. In this paper, we propose and investigate the optimal tuning PID controller of unstable fractional order system by desired transient characteristics using the real interpolation method (RIM). The main advantages of this method are drawn as the followings: 1) Carrying out an investigation of the stable region of coefficients of a PID controller using D- decomposition method. 2) Applying the method to investigate an unstable fractional order system. The rest of this paper is organized as follows. In Section 2 the problem is formulated. Numerical results and discussions are described in Section 3. Conclusions are drawn in Section 4. 2. PROBLEM FORMULATION In this section, Figure 1 illustrates the control system with the negative unity feedback. The mathematical description of this model is presented. Figure 1. Control system with negative unity feedback The transfer function of the PID controller can be formulated as K (s) K K i p d C s s    (1) The transfer function of the plant (in the fractional form) is calculated as 1 0 1 1 0 1 1 1 0 1 1 0 B (s) G(s) ( ) n n m m G n n G m m b s b s b s b s A s a s a s a s a s                         (2) where 𝑚, 𝑛 ∈ 𝑁, 𝑎𝑛𝑑 𝑎 , … , 𝑎 , 𝑏 , … , 𝑏 , 𝛼 𝛼 ⋯ 𝛼 𝛼 0, 𝛽 𝛽 ⋯ 𝛽 𝛽 0 are arbitrary real numbers 𝑎 0, 𝑏 0. The transfer function of PID controller (1) can be rewritten in the rational form as the following 2 K K K ( ) (s) ( ) d p i C C s s B s C A s s     (3) The characteristic equation in this analysis can be expressed as W( ) 1 (s)G(s) s C   (4) Characteristic polynomial is formulated as
  • 3.  ISSN: 2088-8694 Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741 1736   2 P( ) ( ) K K K B ( ) G d p i G s sA s s s s     (5) A gain-phase margin tester (GPMT) can be thought of as a “virtual compensator”, provides information for plotting the boundaries of constant gain margin and phase margin in a parameter plane [14]. The frequency independent GPMT is given as in [15]: (M, ) Me . j t G     (6) For a given IOPID controller parameters K , K , K p i d the closed-loop system is said to be bounded- input bounded-output (BIBO) stable if the quasi-polynomial P(s, K , K , K ) p i d has no roots in the closed right- half of the s-plane (RHP). The stability domain S in the parameter space P with K , K , K p i d being coordinates is the region that for K , K , K p i d S  the roots of quasi-polynomial P(s, K , K , K ) p i d all lie in open left-half of the s-plane (LHP). The boundaries of the stability domain S which are described by real root boundary (RRB), infinite root boundary (IRB) and complex root boundary (CRB) can be determined by the D-decomposition method [15], [16] . These boundaries are defined by the equations P(0,K) 0  , P( ,K) 0   and P( j ,K) 0    for (0, )   , respectively, where P(s,K) is the characteristic function of the closed- loop system and K the vector of controller parameters. 2.1. Determining RRB In applying the descriptions of stability boundaries of the stability domain S to the FOCE in (1), the RRB turns out to be simply a straight line given by P(0, K , K , K ) 0 0, p i d i K    (7) for 0 1 s  in the transfer function of the plant in (2). 2.2. Determining IRB The calculating of the IRB faces with more technical difficulties due to the fractional component. FOCE possesses an infinite number of roots, which cannot be calculated analytically in the general case. However, the asymptotic location of roots far from the origin is well known [17], which may lead to IRB. The objective of this section is to determine the stabilizing region in 𝐾 , 𝐾 plane with given 𝐾 , and values for which the following complex polynomial is Hurwitz:   2 D( ) ( ) ( ) K K K M(s)B ( ) G d p i G s sL s A s s s s     (8) where L(s) and M(s) are given complex fractional order polynomials. When 𝐿 𝑠 𝑀 𝑠 1, the stabilization of Eq. (8) reduces to the standard IOPID stabilization. From (8), we have D( ) 0   . Suppose when s   ,         / t G G L s A s M s s B s c          where t and c are real and complex numbers respectively. We have [16]: (a) If 1 t  , then the boundary does not exist. (b) If 1 t  and c is not real, then the boundary does not exist. (c) If 1 t  and c is real, then            2 lim lim1 1 0 p i d d s s G G N s K s K K s D s K c sL s A s sA s          (9) 1 d K c   (10) The RRB and IRB lines can be obtained from (7) and (10), respectively. 2.3. Determining CRB 
  • 4. Int J Pow Elec & Dri Syst ISSN: 2088-8694  Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan) 1737 To construct the CRB, we substitute s j  into (5) to obtain P(j ) (j ) (j ) (j )B (j ) 0 C G C G A A B         (11) Using D-decomposition to find stability [15]. In the s plane ( ) 2 cos( ) jsin( ) 2 2 j j e           , where  is a real number. The formula (6) can be expressed into a formula with the separate real and imaginary components 2 P(j ) (K K )R ( ) I ( ) K R ( ) R ( ) 0 i d BG AG p BG AG j                       , (12) where RBG , RAG , IAG are the real component of B (j ) G  , the real and imaginary components of (j ) G A  , respectively. Finally, by setting the real and imaginary parts equalized zero the formula (12) leads to the detail form: 2 R ( ) K R ( ) 0 (K K )R ( ) I ( ) 0 AG p BG i d BG AG                 (13) The solution in the (Kp, Ki) plane This is a three-dimensional system in terms of the controller parameters K , K , K p i d . In order to deal with two unknowns K , K p i , the value of Kd will be fixed to find the stability region in the (K , K ) p i plane. Equation (11) rewrite in terms of two unknowns K , K p i . 2 K R ( ) / R ( ) K ( ) / R ( ) K p AG BG i AG BG d I                (14) The above two equations trace out a curve in the (K , K ) p i -plane representing the CRB, for fixed Kd , as  run from 0 to  . The solution in the (Kp, Kd) plane Next, to find the stability region in the (Kp, Kd) plane, the value of Ki will be fixed. Then formula (13) can be rewritten as: 2 K R ( ) / R ( ) K K I ( ) / R ( ) / p AG BG d i AG BG                    (15) The above two equations trace out a curve in the (K , K ) p d -plane representing the CRB, for fixed Ki , as  run from 0 to  . The solution in the (Ki, Kd) plane Next, to find the stability region in the (Ki, Kd) plane, the value of Kd will be fixed. Then formula (13) can be rewritten as: 2 K R ( ) / R ( ) K K I ( ) / R ( ) / p AG BG d i AG BG                    (16) The above two equations trace out a curve in the (K , K ) i d -plane representing the CRB, for fixed Kp , as  run from 0 to  . 3. NUMERICAL SAMPLE AND DISCUSSION Given fractional order transfer function of an unstable bearing system [18] [19],
  • 5.  ISSN: 2088-8694 Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741 1738 2.76 1.81 0.82 6438. G(s) 330.04 84268.85 15869154.14 s s s     (17) Investigation of the stability region of the unstable fractional order transfer function of the bearing system (17) is carried out in the following parts. 3.1. Determining RRB It is important to determine the stability region of the PID controller, tuned for the system (17). The RRB can be determined by (7) as the bellow 0. i K  (18) 3.2. Determining IRB The IRB can be determined according to (9)       2.76 1.81 0 2 .82 330.04 643.8 lim lim1 ) 1 ( 84268.85 15869154.14) p i d s s s K s K K s s sD s s s s            (19) Not exist the IRB. Figure 2. The CRB graph in the K , K plane and K 10. 3.3. Determining CRB  The CRB can be determined by three conditions (13), (14) and (15). Figure 2 shows the stability region of the transfer function (17). The CRB in the (K_p,K_i) plane when K_d=10 is shown in the Figure 2. The cross-line area is a feasible region for the coefficients of the PID controller. The cross-line region demonstrates stability region of K_p,K_i where K_d=10. Obviously, the stability region of PID controller’s coefficients lie in the first quarter of the coordinate [22-25]. Furthermore, Figure 3 shows a more feasible area with five values of 𝐾 . Kp Ki Ki Kp
  • 6. Int J Pow Elec & Dri Syst ISSN: 2088-8694  Determination of all stability region of unstable fractional order system in case of ... (Van-Duc Phan) 1739 Figure 3. The CRB graphs in the K , K plane with 5 values of coefficients K . Figure 3 shows that by increasing the value of the coefficient 𝐾 , the feasible region is expanded. Figure 4. The CRB of the PID coefficients In Figure 4. The distribution of 𝐾 , 𝐾 , 𝐾 in the 3-D system is represented. In more details, we can investigate the stability region of the PID controller’s coefficient separately in the 2-D coordinate plane. In the Figure 4. Figure 5. The CRB in the K , K plane Figure 5 illustrates the stability region of 𝐾 and 𝐾 . Obviously, the stability region is covered the first and fourth quarters of the coordinate system. From the Figure 5, there is a significance that the coefficient 𝐾 2465. Furthermore, The Figure 6 show the stability region in the 𝐾 , 𝐾 plane. The values of the coefficient 𝐾 , 𝐾 are located in the first and fourth quarters, and of course 𝐾 2456. Figure 6. The CRB in the K , K plane
  • 7.  ISSN: 2088-8694 Int J Pow Elec & Dri Syst Vol. 10, No. 4, Dec 2019 : 1734 – 1741 1740 The CRB in the K , K plane shows that the distribution of 𝐾 and 𝐾 Figure 7. The CRB in the K , K plane The results simply lead to the conclusion 2465 0 p i K K        (20) Three parameters , , p i d K K K of the PID controller are determined in four figure 4-7 [22-25]. 4. CONCLUSION In this paper, we propose and investigate optimal tuning PID controller of unstable fractional order system by desired transient characteristics using the real interpolation method (RIM). The research shows that the main advantages of this method are drawn as the followings: 1) Carrying out an investigation of the stable region of coefficients of a PID controller using D-decomposition method; 2) Applying the method to investigate an unstable fractional order system. ACKNOWLEDGEMENTS This research was supported by National Key Laboratory of Digital Control and System Engineering (DCSELAB), HCMUT, VNU-HCM, Vietnam. REFERENCES [1] Heydarpoor, Saeed, and Mohammad Tabatabaei, "Velocity control of a DC motor based on fractional order PI and IMC-based fractional order controllers," International Journal of Advanced Mechatronic Systems, vol. 7, no. 1, 2016. doi:10.1504/ijamechs.2016.079650. [2] Zheng, Shiqi, "Robust stability of fractional order system with general interval uncertainties,” Systems & Control Letters, vol. 99, pp. 1-8, 2017. doi:10.1016/j.sysconle.2016.11.001. [3] Vinagre, Blas M., et al, "Fractional PID controllers for industry application. A brief introduction," Journal of Vibration and Control, vol. 13, no. 9-10, pp. 1419-1429, 2007. doi:10.1177/1077546307077498. [4] Monje, Concepción A., et al., "Tuning and auto-tuning of fractional order controllers for industry applications," Control Engineering Practice, vol. 16, no. 7, pp. 798-812, 2008. doi:10.1016/j.conengprac.2007.08.006. [5] Chen, Yangquan, et al., "Practical tuning rule development for fractional order proportional and integral controllers," Journal of Computational and Nonlinear Dynamics, vol. 3, no. 2, 2008. doi:10.1115/1.2833934. [6] Petráš, Ivo, "Tuning and implementation methods for fractional-order controllers," Fractional Calculus and Applied Analysis, vol. 15, no. 2, 2012. doi:10.2478/s13540-012-0021-4. [7] Li, Hongsheng, Ying Luo, and Yangquan Chen, "A fractional order proportional and derivative (FOPD) motion controller: Tuning rule and experiments," IEEE Transactions on Control Systems Technology, vol. 18, no. 2, 516- 20, 2010. doi:10.1109/tcst.2009.2019120. [8] Luo, Ying, Chunyang Wang, and Yangquan Chen, "Tuning fractional order proportional integral controllers for fractional order systems," 2009 Chinese Control and Decision Conference, vol. 6, 2009. doi:10.1109/ccdc.2009.5195101.
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