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International Journal of Engineering Research and Development
ISSN: 2278-067X, Volume 1, Issue 12 (July 2012), PP. 69-74
www.ijerd.com

    Comparison of LQR and PD controller for stabilizing Double
                   Inverted Pendulum System
                              Narinder Singh1, Sandeep Kumar Yadav2
          Department of control and instrumentation Engineering, NIT Jalandhar, Punjab 144011 India



Abstract—this paper presented comparison of the time specification performance between two type of controller for a
Double Inverted Pendulum system. Double Inverted Pendulum is a non-linear ,unstable and fast reaction system. DIP is
stable when its two pendulums allocated in vertically position and have no oscillation and movement and also inserting
force should be zero. The objective is to determine the control strategy that to delivers better performance with respect to
pendulum angle’s and cart position. In this paper simple multi PD controller designed on the theory of pole placement
and its performance is compared with Linear Quadratic Regulator controller using MATLAB and Simulink.

Keywords––Double Inverted Pendulum; LQR; PD Controller; pole placement; MATLAB

                                                 I. INTRODUCTION
          Te inverted pendulum offers a very good example for control engineers to verify a modern control theory. This can
be explained by the facts that inverted pendulum is marginally stable, in control sense, has distinctive time variant
mathematical model. The double inverted pendulum is a highly nonlinear and open-loop unstable system. The inverted
pendulum system usually used to test the effect of the control policy, and it is also an ideal experimental instrument in the
study of control theory [1, 2]. To stabilize a double inverted pendulum is not only a challenging problem but also a useful
way to show the power of the control method (PID controller, neural network, FLC, genetics algorithm, etc.).

          In this paper common control approaches such as the linear quadratic controller (LQR) and PD controller based on
a pole placement technique to overcome the problem of this system require a good knowledge of the system and accurate
tuning obtain good performance [3-5]. This paper presents investigations of performance comparison between modern
control and PD control for a double inverted pendulum system. Performance of both controller strategies with respect to
pendulums angle and cart position is examined.

                        II. MODELING OF DOUBLE INVERTED PENDULUM
           To control this system, its dynamic behavior must be analyzed first. The dynamic behavior is the changing rate of
the status and position of the double inverted pendulum proportionate to the force applied. This relationship can be explained
using a series of differential equations called the motion equations ruling over the pendulum response to the applied force.
The double inverted pendulum is shown in Fig 1. The meanings and values of the parameters for inverted pendulum are
given in Table 1. [4]




                                    Fig1: schematic diagram of Double Inverted Pendulum

To derive its equations of motion, one of the possible ways is to use Lagrange equations [6]
                                                                                𝑑 𝑑𝐿      𝑑𝐿
                                                                                        −      = 𝑄𝑖                       (1)
                                                                                𝑑𝑡 𝑑𝑞 𝑖   𝑑𝑞 𝑖



                                                             69
Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System

                                      TABLE I : P ARAMETERS OF DOUBLE INVERTED PENDULUM
                                 M(m1,m2,m3)         Mass of thecart,( first pole, second pole,
                                                     joint)
                                                     5.8kg(1.5kg,.5kg,.75kg)
                                 θ1,θ2               The angle between pole 1(2) and vertical
                                                     direction (rad)
                                 L1(l1), L2(l2)      Length of pendulum first(2l1) and length of
                                                     second pendulum (2l2) ,1m,1.5m
                                 g                   Center of gravity 9.8m/s2
                                 F                   Force applied to cart

    Where L = T - V is a Lagrangian, Q is a vector of generalized forces (or moments) acting in the direction of generalized
coordinates q and not accounted for in formulation of kinetic energy T and potential energy V. Kinetic and potential energies
of the system are given by the sum of energies of cart and pendulums.
         1                               2                                 2  1          2
     𝑇=     𝑚0 + 𝑚1 + 𝑚2 + 𝑚3 𝑥 2 +        𝑚1 𝑙1 2 + 2𝑚2 𝑙1 2 + 2𝑚3 𝑙1 2 𝜃1 + 𝑚2 𝑙2 2 𝜃2 + 𝑚1 𝑙1 + 2𝑚2 𝑙1 +
         2                                   3                                       6
2𝑚3 𝑙1 𝑥 𝜃1 𝑐𝑜𝑠 𝜃1 + 𝑚2 𝑙2 𝑥 𝜃2 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝑐𝑜𝑠 𝜃1 − 𝜃2 𝜃1 𝜃2                                                         (2)
  𝑉 = 𝑚1 𝑔𝑙1 cos𝜃1 + 2𝑚3 𝑔𝑙1 cos𝜃1 + 𝑚2 𝑔(2𝑙1 cos𝜃1 + 𝑙2 cos𝜃2 )                                                     (3)
 Thus the Lagrangianof the system is given
      1                                2                                 2 1          2
  𝐿=      𝑚0 + 𝑚1 + 𝑚2 + 𝑚3 𝑥 2 +        𝑚1 𝑙1 2 + 2𝑚2 𝑙1 2 + 2𝑚3 𝑙1 2 𝜃1 + 𝑚2 𝑙2 2 𝜃2 +                𝑚1 𝑙1 + 2𝑚2 𝑙1 +
         2                                   3                                       6
2𝑚3 𝑙1 𝑥 𝜃1 𝑐𝑜𝑠 𝜃1 + 𝑚2 𝑙2 𝑥 𝜃2 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝑐𝑜𝑠 𝜃1 − 𝜃2 𝜃1 𝜃2 − 𝑚1 𝑔𝑙1 cos𝜃1 − 2𝑚3 𝑔𝑙1 cos𝜃1 − 𝑚2 𝑔(2𝑙1 cos𝜃1 +
 𝑙2 cos𝜃2 )         (4)
       Differentiating the Lagrangian by and θ and θ yields Lagrange equation (1) as:
                                                                                            𝑑 𝑑𝐿      𝑑𝐿
                                                                                                  −       =0                          (5)
                                                                                           𝑑𝑡 𝑑𝜃1     𝑑𝜃1
                                                                                            𝑑 𝑑𝐿      𝑑𝐿
                                                                                                  −       =0                          (6)
                                                                                           𝑑𝑡 𝑑𝜃2     𝑑𝜃2
Or explicitly:
   4                                                                                                                        2
       𝑚 𝑙 2 + 4𝑚2 𝑙1 2 + 4𝑚3 𝑙1 2 𝜃1 + 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2𝑚3 𝑙1 𝑥 cos𝜃1 + 2𝑚2 𝑙1 𝑙2 𝜃2 𝑐𝑜𝑠 𝜃1 − 𝜃2 + 2𝑚2 𝑙1 𝑙2 𝜃2 𝑠𝑖𝑛 𝜃1 −
   3 1 1
  𝜃2 − 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2𝑚3 𝑙1 𝑔 sin𝜃1 = 0                                 (7)
                                                1                              2
   𝑚2 𝑙2 𝑥 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝜃1 𝑐𝑜𝑠 𝜃1 − 𝜃2 + 3 𝑚2 𝑙2 2 𝜃2 − 2𝑚2 𝑙1 𝑙2 𝜃1 𝑠𝑖𝑛 𝜃1 − 𝜃2 − 𝑚2 𝑙2 𝑔 sin𝜃2 = 0                        (8)
Lagrange equation for the DICP system can be written in a more compact matrix form:
D(θ) 𝜃+C(θ,𝜃) 𝜃 + G(θ) = Hu                         (9)
The stationary point of the system is (𝑥, 𝜃1 , 𝜃2 , 𝑥, 𝜃1 , 𝜃2, 𝑥) = (0, 0, 0, 0, 0, 0, 0), introduce small deviation around a stationary
point and Taylor series expansion; the stable control process of the Double Inverted Pendulums are usually cos(θ 1 – θ2)=1,
sin (θ1 – θ2), cos(θ1)≅cos(θ2)≅1, sin(θ1)≅θ1, sinθ2≅ θ2 . Linearization is made at balance position; we can get the linear time
invariant state space model [7].
     𝑥      0       0          0     0 0 0 𝑥               0
    𝜃1      0       0          0     0 0 0 𝜃1              0
   𝜃2       0       0          0     0 0 0 𝜃2              0
        =                                         +                𝑢(𝑡)
     𝑥      0       0          0     0 0 0 𝑥               1
    𝜃1      0 14.2545 −4.0090 0 0 0           𝜃1      1.1818
   𝜃2       0 −14.2545 21.1077 0 0 0 𝜃2               0.1818
            100000 𝑥              0
  𝑦 𝑡 = 0 1 0 0 0 0 𝜃1 + 0 𝑢(𝑡)                       (10)
            0 0 1 0 0 0 𝜃2        0

                           III. ANALYSIS OF DOUBLE INVERTED PENDULUM
         After obtaining the mathematical model of the system features, we need to analyze the stability; controllability and
Observability of systems in order to further understand the characteristics of the system [8].

A. Stability
          If the closed-loop poles are all located in the left half of “s” plane, the system must be stable, otherwise the system
is unstable. In MATLAB, to strike a linear time-invariant system, the characteristic roots can be obtain by eig (a,b) function.
According to the sufficient and necessary conditions for stability of the system, we can see the inverted pendulum system is
unstable

B. Controllability
          A system is said to be controllable if any initial state x(t 0 ) or x0 can be transfer to any final state x( tf) in a finite
time interval (tf - t0), t ≥ 0 by some control u.
The test of controllability due to Kalman if system is completely controllable if and only if the rank of the composite matrix
Qc is n.

                                                                  70
Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System

Qc = [B AB … … … … An-1B]                         (10)
      C. Observability
    A system is said to be observable if every state x 0 can be exactly determined from the measurement of the output „y‟ over
a finite interval of time 0 ≤ t ≥ t f.
    The test of controllability due to Kalman if system is completely observable if and only if the rank of composite matrix is
n where
    Oc = [CT AT CT (AT )2CT…………….(AT)n-1 CT]                  (11)

                         IV. DESIGN OF LINEAR QUADRATIC REGULATOR
   This leads to the Linear Quadratic Regulator (LQR) system dealing with state regulation, output regulation, and tracking.
Broadly speaking, we are interested in the design of optimal linear systems with quadratic performance indices [9].
   We shall now consider the optimal regulator problem that, given the system equation.
      𝑥(𝑡) = A x(t) + Bu(t)
     Y(t) = C x(t) + D u(t)               (12)
     Determine the matrix K of the optimal control vector.
      𝑢 𝑡 = −𝐾𝑥 𝑡                    (13)
     So as to minimize the performance index
           ∞
     J = 0 (𝑥 𝑇 𝑡 𝑄𝑥 𝑡 + 𝑢 𝑇 𝑡 𝑅𝑢 𝑡 )𝑑𝑡                (14)
   Where Q is a positive-semi definite and R is a positive-definite matrix. The matrices Q and R determine the relative
importance of the error. Here the elements of the matrix K are determined so as to minimize the performance index.
   Then 𝑢 𝑡 = −𝐾𝑥 𝑡 = −𝑅−1 𝐵 𝑇 𝑃𝑥(𝑡) is optimal for any initial x(0) state.




                                        Fig 2: Full state feedback representation of DIP

Where P (t) is the solution of Riccati equation, K is the linear optimal feedback matrix. Now we only need to solve the
Riccati equation.
    𝐴 𝑇 𝑃 + 𝑃𝐴 − 𝑃𝐵𝑅−1 𝐵 𝑇 𝑃 + 𝑄 = 0            (15)
   Where Q and R chose as Q = diag ([10 60 80 0 0 0]) and R = 1.
   Therefore,
   K= −𝑅−1 𝐵 𝑇 𝑃 = [10 275.2453 -515.6502 16.2044 22.1046 -111.9285]

                                      V. DESIGN OF PD CONTROLLER
           A Proportional-Derivative (PD) controller is a control loop feedback mechanism used in process control type
industrial. A PD controller calculates an “error” value as the difference between a measured process variable and a desired
set point. The controller attempts to minimize the error by adjusting the process input. PD controller calculation involves two
parameters values proportional (P) and derivative (D). Proportional values is determines the reaction to the current error,
derivative values determines the reaction rate at which the error has been changing [5~10].




                                           Fig3: Block diagram of DIP PD controller


                                                             71
Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System

          PD controller is combination of proportional plus derivative controller. It consists to a single input three output of
a double inverted pendulum system. This is the case of stabilization of a double inverted pendulum at is x = 𝜃1 = 𝜃2 = 0,
which is a physical unbalance position. So integral action will result in instability condition of control system and a simple
PD controller is more adaptive. Then we have used a three (multi) PD controller.
The transfer function of PD controller is (Kp + KdS) i.e. PD1, PD2, and PD3 transfer functions are respectively (K1 +K2S),
(K3 +K4S) and (K5 +K6S).




                                            Fig4: The structure of DIP PD controller

        We now use a pole placement technique of state feedback control system to determine the 6 PD control parameter.
When assume that desired closed pole are -2.1±2.1425j, -5, -5, -5, -5. We can obtain the parameter of PD controller by using
the MATLAB i.e.
   K1=131.4941, K2=-23.4289, K3=-549.4167
   K4=-124.6183, K5=23.0785, K6=29.2327

                                        VI. SIMULATION AND RESULT
         The system under consideration and the proposed controllers are modeled and simulated in the
MATLAB/Simulink environment. The step response performance of the two controllers is compared fig.5 shows the step
response of the system under consideration in absence of a controller and is found to be unstable.




                              Fig5: Step response of Double Inverted Pendulum without controller




                                                              72
Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System




                     Fig6: Step response of Pendulum angles and cart position by using LQR controller.




                                 Fig7. Step response of cart position by using PD controller




                                Fig8: The response of first pendulum angle by PD controller




                              Fig9: The response of second pendulum angle by PD controller

          The time response specification for the system under consideration equipped with the proposed controllers are
given in Tables 2, 3 and 4.




                                                           73
Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System

                                                             TABLE 2
                                         Time response        LQR             PD
                                         specification        controller      controller
                                         Settling     time    3.05 s          3s
                                         (Ts)
                                         Rise time (Tr)       0.51s           .15s
                                         Peak overshoot       20%             5.8%
                                         steady      state    0.02            0.0117
                                         error (ess)
SUMMARY OF THE PERFORMANCE CHARACTERISTICS FOR CART POSITION


                                                             TABLE 3
                                         Time response        LQR             PD
                                         specification        controller      controller
                                         Settling     time    4.68S           2.876S
                                         (Ts)
                                         Rise time (Tr)       0.21S           0.17S
                                         Peak overshoot       1.6%            7.5%
                                         Steady      state    0               0
                                         error (ess)
SUMMARY OF THE PERFORMANCE CHARACTERISTICS FOR FIRST PENDULUM‟S ANGLE


                                                             TABLE 4
                                       Time       response     LQR             PD
                                       specification           controller      controller
                                       Settling time (TS)      4.67S           3.08S
                                       Rise time (Tr)          0.907S          0.62S
                                       Peak overshoot          5%              7%
                                       Steady state error      0               0
                                       (ess)
SUMMARY OF THE PERFORMANCE CHARACTERISTICS OF SECOND PENDULUM‟S ANGLE

          From both controller LQR and PD controller‟s result, It is clear that both are successfully designed but PD
controller exhibits better response and performance.

                                                   VII. CONCLUSION
          In this paper, LQR and PD controller are successfully designed for a Double Inverted Pendulum system. Based on
the results, both controllers are capable of controlling the double inverted pendulum‟s angles and the cart position of the
linearized system. However, the simulation result shows that PD controller has a better performance as compared to the LQR
controller in controlling the Double Inverted Pendulum system.

                                                      REFERENCES
[1].      Yan xueli, JIANG hanhong. “Control method study on a single inverted pendulum in a simulink environment”. Measure and
          control technology, 2005, 24(07):37-39.
[2].      ZHAN G Hongli         “simulation of virtual inverted pendulum based on MATLAB”. Machine Building and Automation, Dec
          2004,33(6):103-105
[3].      Chen Wei Ji, Fang Lei, and Lei Kam Kin, “Fuzzy logic controller for an inverted pendulum,” system and control in Aerospace
          and Astronautics, 2008. ISSCAA 2008. 2 nd international symposium on, vol.,no.,pp.1-3,10-12 Dec 2008.
[4].      Gugao Company, GT-400-SV inverted pendulum users’ guide. 2002.
[5].      Yingjun Sang, Yuanyuan Fan, Bin Liu, “double inverted pendulum control based on three loop PID and improved BP neural
          network,” second international conference on digital manufacturing & Automation,2011,456-459.
[6].      Bogdanov Alexander, 2004, “Optimal Control of a Double Inverted Pendulum on a Cart”, Technical Report CSE-04-006.Y.
[7].      A.L. Fradkov, P. Y. Guzenko, D. J. Hill, A. Y. Pogromsky. “Speed gradient control and passivity of nonlinear oscillators,”
          Proc. of IFAC symposium on Control of Nonlinear Systems, Lake Tahoe. 1995:655-659.
[8].      Jian Pan, Jun Wang “The study of two kinds control strategy based on inverted pendulum”. Modern electronic
          technology.2008.1.
[9].      Desineni subbaram Naidu, “Optimal control system”, Idaho state university. Pocatello. Idaho, USA, June 2002.
[10].     Syed Hasan Saeed, “Automatic control system”, S.K.KATARIA & SONS August 2002.




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  • 1. International Journal of Engineering Research and Development ISSN: 2278-067X, Volume 1, Issue 12 (July 2012), PP. 69-74 www.ijerd.com Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System Narinder Singh1, Sandeep Kumar Yadav2 Department of control and instrumentation Engineering, NIT Jalandhar, Punjab 144011 India Abstract—this paper presented comparison of the time specification performance between two type of controller for a Double Inverted Pendulum system. Double Inverted Pendulum is a non-linear ,unstable and fast reaction system. DIP is stable when its two pendulums allocated in vertically position and have no oscillation and movement and also inserting force should be zero. The objective is to determine the control strategy that to delivers better performance with respect to pendulum angle’s and cart position. In this paper simple multi PD controller designed on the theory of pole placement and its performance is compared with Linear Quadratic Regulator controller using MATLAB and Simulink. Keywords––Double Inverted Pendulum; LQR; PD Controller; pole placement; MATLAB I. INTRODUCTION Te inverted pendulum offers a very good example for control engineers to verify a modern control theory. This can be explained by the facts that inverted pendulum is marginally stable, in control sense, has distinctive time variant mathematical model. The double inverted pendulum is a highly nonlinear and open-loop unstable system. The inverted pendulum system usually used to test the effect of the control policy, and it is also an ideal experimental instrument in the study of control theory [1, 2]. To stabilize a double inverted pendulum is not only a challenging problem but also a useful way to show the power of the control method (PID controller, neural network, FLC, genetics algorithm, etc.). In this paper common control approaches such as the linear quadratic controller (LQR) and PD controller based on a pole placement technique to overcome the problem of this system require a good knowledge of the system and accurate tuning obtain good performance [3-5]. This paper presents investigations of performance comparison between modern control and PD control for a double inverted pendulum system. Performance of both controller strategies with respect to pendulums angle and cart position is examined. II. MODELING OF DOUBLE INVERTED PENDULUM To control this system, its dynamic behavior must be analyzed first. The dynamic behavior is the changing rate of the status and position of the double inverted pendulum proportionate to the force applied. This relationship can be explained using a series of differential equations called the motion equations ruling over the pendulum response to the applied force. The double inverted pendulum is shown in Fig 1. The meanings and values of the parameters for inverted pendulum are given in Table 1. [4] Fig1: schematic diagram of Double Inverted Pendulum To derive its equations of motion, one of the possible ways is to use Lagrange equations [6] 𝑑 𝑑𝐿 𝑑𝐿 − = 𝑄𝑖 (1) 𝑑𝑡 𝑑𝑞 𝑖 𝑑𝑞 𝑖 69
  • 2. Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System TABLE I : P ARAMETERS OF DOUBLE INVERTED PENDULUM M(m1,m2,m3) Mass of thecart,( first pole, second pole, joint) 5.8kg(1.5kg,.5kg,.75kg) θ1,θ2 The angle between pole 1(2) and vertical direction (rad) L1(l1), L2(l2) Length of pendulum first(2l1) and length of second pendulum (2l2) ,1m,1.5m g Center of gravity 9.8m/s2 F Force applied to cart Where L = T - V is a Lagrangian, Q is a vector of generalized forces (or moments) acting in the direction of generalized coordinates q and not accounted for in formulation of kinetic energy T and potential energy V. Kinetic and potential energies of the system are given by the sum of energies of cart and pendulums. 1 2 2 1 2 𝑇= 𝑚0 + 𝑚1 + 𝑚2 + 𝑚3 𝑥 2 + 𝑚1 𝑙1 2 + 2𝑚2 𝑙1 2 + 2𝑚3 𝑙1 2 𝜃1 + 𝑚2 𝑙2 2 𝜃2 + 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2 3 6 2𝑚3 𝑙1 𝑥 𝜃1 𝑐𝑜𝑠 𝜃1 + 𝑚2 𝑙2 𝑥 𝜃2 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝑐𝑜𝑠 𝜃1 − 𝜃2 𝜃1 𝜃2 (2) 𝑉 = 𝑚1 𝑔𝑙1 cos𝜃1 + 2𝑚3 𝑔𝑙1 cos𝜃1 + 𝑚2 𝑔(2𝑙1 cos𝜃1 + 𝑙2 cos𝜃2 ) (3) Thus the Lagrangianof the system is given 1 2 2 1 2 𝐿= 𝑚0 + 𝑚1 + 𝑚2 + 𝑚3 𝑥 2 + 𝑚1 𝑙1 2 + 2𝑚2 𝑙1 2 + 2𝑚3 𝑙1 2 𝜃1 + 𝑚2 𝑙2 2 𝜃2 + 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2 3 6 2𝑚3 𝑙1 𝑥 𝜃1 𝑐𝑜𝑠 𝜃1 + 𝑚2 𝑙2 𝑥 𝜃2 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝑐𝑜𝑠 𝜃1 − 𝜃2 𝜃1 𝜃2 − 𝑚1 𝑔𝑙1 cos𝜃1 − 2𝑚3 𝑔𝑙1 cos𝜃1 − 𝑚2 𝑔(2𝑙1 cos𝜃1 + 𝑙2 cos𝜃2 ) (4) Differentiating the Lagrangian by and θ and θ yields Lagrange equation (1) as: 𝑑 𝑑𝐿 𝑑𝐿 − =0 (5) 𝑑𝑡 𝑑𝜃1 𝑑𝜃1 𝑑 𝑑𝐿 𝑑𝐿 − =0 (6) 𝑑𝑡 𝑑𝜃2 𝑑𝜃2 Or explicitly: 4 2 𝑚 𝑙 2 + 4𝑚2 𝑙1 2 + 4𝑚3 𝑙1 2 𝜃1 + 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2𝑚3 𝑙1 𝑥 cos𝜃1 + 2𝑚2 𝑙1 𝑙2 𝜃2 𝑐𝑜𝑠 𝜃1 − 𝜃2 + 2𝑚2 𝑙1 𝑙2 𝜃2 𝑠𝑖𝑛 𝜃1 − 3 1 1 𝜃2 − 𝑚1 𝑙1 + 2𝑚2 𝑙1 + 2𝑚3 𝑙1 𝑔 sin𝜃1 = 0 (7) 1 2 𝑚2 𝑙2 𝑥 𝑐𝑜𝑠𝜃2 + 2𝑚2 𝑙1 𝑙2 𝜃1 𝑐𝑜𝑠 𝜃1 − 𝜃2 + 3 𝑚2 𝑙2 2 𝜃2 − 2𝑚2 𝑙1 𝑙2 𝜃1 𝑠𝑖𝑛 𝜃1 − 𝜃2 − 𝑚2 𝑙2 𝑔 sin𝜃2 = 0 (8) Lagrange equation for the DICP system can be written in a more compact matrix form: D(θ) 𝜃+C(θ,𝜃) 𝜃 + G(θ) = Hu (9) The stationary point of the system is (𝑥, 𝜃1 , 𝜃2 , 𝑥, 𝜃1 , 𝜃2, 𝑥) = (0, 0, 0, 0, 0, 0, 0), introduce small deviation around a stationary point and Taylor series expansion; the stable control process of the Double Inverted Pendulums are usually cos(θ 1 – θ2)=1, sin (θ1 – θ2), cos(θ1)≅cos(θ2)≅1, sin(θ1)≅θ1, sinθ2≅ θ2 . Linearization is made at balance position; we can get the linear time invariant state space model [7]. 𝑥 0 0 0 0 0 0 𝑥 0 𝜃1 0 0 0 0 0 0 𝜃1 0 𝜃2 0 0 0 0 0 0 𝜃2 0 = + 𝑢(𝑡) 𝑥 0 0 0 0 0 0 𝑥 1 𝜃1 0 14.2545 −4.0090 0 0 0 𝜃1 1.1818 𝜃2 0 −14.2545 21.1077 0 0 0 𝜃2 0.1818 100000 𝑥 0 𝑦 𝑡 = 0 1 0 0 0 0 𝜃1 + 0 𝑢(𝑡) (10) 0 0 1 0 0 0 𝜃2 0 III. ANALYSIS OF DOUBLE INVERTED PENDULUM After obtaining the mathematical model of the system features, we need to analyze the stability; controllability and Observability of systems in order to further understand the characteristics of the system [8]. A. Stability If the closed-loop poles are all located in the left half of “s” plane, the system must be stable, otherwise the system is unstable. In MATLAB, to strike a linear time-invariant system, the characteristic roots can be obtain by eig (a,b) function. According to the sufficient and necessary conditions for stability of the system, we can see the inverted pendulum system is unstable B. Controllability A system is said to be controllable if any initial state x(t 0 ) or x0 can be transfer to any final state x( tf) in a finite time interval (tf - t0), t ≥ 0 by some control u. The test of controllability due to Kalman if system is completely controllable if and only if the rank of the composite matrix Qc is n. 70
  • 3. Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System Qc = [B AB … … … … An-1B] (10) C. Observability A system is said to be observable if every state x 0 can be exactly determined from the measurement of the output „y‟ over a finite interval of time 0 ≤ t ≥ t f. The test of controllability due to Kalman if system is completely observable if and only if the rank of composite matrix is n where Oc = [CT AT CT (AT )2CT…………….(AT)n-1 CT] (11) IV. DESIGN OF LINEAR QUADRATIC REGULATOR This leads to the Linear Quadratic Regulator (LQR) system dealing with state regulation, output regulation, and tracking. Broadly speaking, we are interested in the design of optimal linear systems with quadratic performance indices [9]. We shall now consider the optimal regulator problem that, given the system equation. 𝑥(𝑡) = A x(t) + Bu(t) Y(t) = C x(t) + D u(t) (12) Determine the matrix K of the optimal control vector. 𝑢 𝑡 = −𝐾𝑥 𝑡 (13) So as to minimize the performance index ∞ J = 0 (𝑥 𝑇 𝑡 𝑄𝑥 𝑡 + 𝑢 𝑇 𝑡 𝑅𝑢 𝑡 )𝑑𝑡 (14) Where Q is a positive-semi definite and R is a positive-definite matrix. The matrices Q and R determine the relative importance of the error. Here the elements of the matrix K are determined so as to minimize the performance index. Then 𝑢 𝑡 = −𝐾𝑥 𝑡 = −𝑅−1 𝐵 𝑇 𝑃𝑥(𝑡) is optimal for any initial x(0) state. Fig 2: Full state feedback representation of DIP Where P (t) is the solution of Riccati equation, K is the linear optimal feedback matrix. Now we only need to solve the Riccati equation. 𝐴 𝑇 𝑃 + 𝑃𝐴 − 𝑃𝐵𝑅−1 𝐵 𝑇 𝑃 + 𝑄 = 0 (15) Where Q and R chose as Q = diag ([10 60 80 0 0 0]) and R = 1. Therefore, K= −𝑅−1 𝐵 𝑇 𝑃 = [10 275.2453 -515.6502 16.2044 22.1046 -111.9285] V. DESIGN OF PD CONTROLLER A Proportional-Derivative (PD) controller is a control loop feedback mechanism used in process control type industrial. A PD controller calculates an “error” value as the difference between a measured process variable and a desired set point. The controller attempts to minimize the error by adjusting the process input. PD controller calculation involves two parameters values proportional (P) and derivative (D). Proportional values is determines the reaction to the current error, derivative values determines the reaction rate at which the error has been changing [5~10]. Fig3: Block diagram of DIP PD controller 71
  • 4. Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System PD controller is combination of proportional plus derivative controller. It consists to a single input three output of a double inverted pendulum system. This is the case of stabilization of a double inverted pendulum at is x = 𝜃1 = 𝜃2 = 0, which is a physical unbalance position. So integral action will result in instability condition of control system and a simple PD controller is more adaptive. Then we have used a three (multi) PD controller. The transfer function of PD controller is (Kp + KdS) i.e. PD1, PD2, and PD3 transfer functions are respectively (K1 +K2S), (K3 +K4S) and (K5 +K6S). Fig4: The structure of DIP PD controller We now use a pole placement technique of state feedback control system to determine the 6 PD control parameter. When assume that desired closed pole are -2.1±2.1425j, -5, -5, -5, -5. We can obtain the parameter of PD controller by using the MATLAB i.e. K1=131.4941, K2=-23.4289, K3=-549.4167 K4=-124.6183, K5=23.0785, K6=29.2327 VI. SIMULATION AND RESULT The system under consideration and the proposed controllers are modeled and simulated in the MATLAB/Simulink environment. The step response performance of the two controllers is compared fig.5 shows the step response of the system under consideration in absence of a controller and is found to be unstable. Fig5: Step response of Double Inverted Pendulum without controller 72
  • 5. Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System Fig6: Step response of Pendulum angles and cart position by using LQR controller. Fig7. Step response of cart position by using PD controller Fig8: The response of first pendulum angle by PD controller Fig9: The response of second pendulum angle by PD controller The time response specification for the system under consideration equipped with the proposed controllers are given in Tables 2, 3 and 4. 73
  • 6. Comparison of LQR and PD controller for stabilizing Double Inverted Pendulum System TABLE 2 Time response LQR PD specification controller controller Settling time 3.05 s 3s (Ts) Rise time (Tr) 0.51s .15s Peak overshoot 20% 5.8% steady state 0.02 0.0117 error (ess) SUMMARY OF THE PERFORMANCE CHARACTERISTICS FOR CART POSITION TABLE 3 Time response LQR PD specification controller controller Settling time 4.68S 2.876S (Ts) Rise time (Tr) 0.21S 0.17S Peak overshoot 1.6% 7.5% Steady state 0 0 error (ess) SUMMARY OF THE PERFORMANCE CHARACTERISTICS FOR FIRST PENDULUM‟S ANGLE TABLE 4 Time response LQR PD specification controller controller Settling time (TS) 4.67S 3.08S Rise time (Tr) 0.907S 0.62S Peak overshoot 5% 7% Steady state error 0 0 (ess) SUMMARY OF THE PERFORMANCE CHARACTERISTICS OF SECOND PENDULUM‟S ANGLE From both controller LQR and PD controller‟s result, It is clear that both are successfully designed but PD controller exhibits better response and performance. VII. CONCLUSION In this paper, LQR and PD controller are successfully designed for a Double Inverted Pendulum system. Based on the results, both controllers are capable of controlling the double inverted pendulum‟s angles and the cart position of the linearized system. However, the simulation result shows that PD controller has a better performance as compared to the LQR controller in controlling the Double Inverted Pendulum system. REFERENCES [1]. Yan xueli, JIANG hanhong. “Control method study on a single inverted pendulum in a simulink environment”. Measure and control technology, 2005, 24(07):37-39. [2]. ZHAN G Hongli “simulation of virtual inverted pendulum based on MATLAB”. Machine Building and Automation, Dec 2004,33(6):103-105 [3]. Chen Wei Ji, Fang Lei, and Lei Kam Kin, “Fuzzy logic controller for an inverted pendulum,” system and control in Aerospace and Astronautics, 2008. ISSCAA 2008. 2 nd international symposium on, vol.,no.,pp.1-3,10-12 Dec 2008. [4]. Gugao Company, GT-400-SV inverted pendulum users’ guide. 2002. [5]. Yingjun Sang, Yuanyuan Fan, Bin Liu, “double inverted pendulum control based on three loop PID and improved BP neural network,” second international conference on digital manufacturing & Automation,2011,456-459. [6]. Bogdanov Alexander, 2004, “Optimal Control of a Double Inverted Pendulum on a Cart”, Technical Report CSE-04-006.Y. [7]. A.L. Fradkov, P. Y. Guzenko, D. J. Hill, A. Y. Pogromsky. “Speed gradient control and passivity of nonlinear oscillators,” Proc. of IFAC symposium on Control of Nonlinear Systems, Lake Tahoe. 1995:655-659. [8]. Jian Pan, Jun Wang “The study of two kinds control strategy based on inverted pendulum”. Modern electronic technology.2008.1. [9]. Desineni subbaram Naidu, “Optimal control system”, Idaho state university. Pocatello. Idaho, USA, June 2002. [10]. Syed Hasan Saeed, “Automatic control system”, S.K.KATARIA & SONS August 2002. 74