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Pole -Placement
     Design
        &
State Observer
                Presented by:-
         Er. Sanyam S.
       Saini
               ME(I&C) Regular
Outlines

 • Servo Design: Introduction of the
   reference Input by Feed forward Control

 • State Feedback with Integral Control
Servo Design: Introduction of the
Reference Input by Feed Forward Control
  The characteristics Equation of the Closed –Loop Control System is
 chosen so as to give satisfactory Transient to disturbances.

  However, no mention is made of a reference i/p or a design
 consideration to yield good transient response with respect to
 command changes.

 In general, both of these considerations should be taken into account in
 the designing of control system.

 This can be done by the proper introduction of the references i/p into
 the system equations.
Continued…….
Consider the completely controllable SISO LTI system with nth – order state
variable model
                     
                     x(t) = Ax(t) + bu(t) …………….…………………(i)
                     y(t) = cx(t)         …………….…..………….…(ii)
We assume that all the n state variables can be accurately measured at all
times. Implementation of appropriately designed Control Law of the form.

                      u(t) = - kx(t)
Let us now assume that for the system given by equs.(i & ii), the desired
steady- state value of the controllable variable y(t) is a constant reference
input r.
For this servo system, the desired equilibrium state x s is a constant point in
state space & is governed by the equations.

                       cx s = r        …………….…..………………………………(iii)
Continued…….
We can formulate this command-following problem as a ”Shifted Regulator
Problem”, by shifting the origin of the state space to the equilibrium point x s .

                       0 = Axs + bu s             …………….………..………….…(iv)
Assuming for the present that a   u s exists that satisfies equns. (iii & iv)
                                  us
                       ~(t) = u(t) - u
                       u               s
                       ~(t) = x(t) - x
                       x                      s           .………..………….…..(v)
                       ~(t) = y(t) - r
                       y
The shifted variables satisfy the equations

                        
                        ~ = A~ + b~
                        x    x    u                       .………..………….…..(vi)

                        ~ = c~
                        y x                               .………..……………...(vii)
Continued…….
This system possesses a time – invariant asymptotically stable control law
                          ~ = -k~
                          u     x                          .………..………….…..(viii)
In terms of the original state variables , total control effort

                 u(t)      -kx(t)        us       kxs       .………..….……….…..(ix)
              (A - bk)x s         b(us          kxs )      0
                                 or
              xs         ( A bk ) 1 b(us                kxs )
                                            1
        cx s r             c( A bk ) b(us kxs )
 The equation has a unique solutions for     (us kxs ) ;

                     (u s kx s ) Nr                        .………..………….…..(x)
Continued…….
Where N is a scalar feedforword gain, given by

                 N -1          c( A      bk ) 1 b
The control law (ix), therefore takes the form

                 u(t)         - kx(t)        Nr
                                                    w
        r                            u                   y
                N                                PLANT
                          +     _

                                                    x
                                         K
               Control Configuration of a Servo System
Numerical Problem
Consider a Attitude Control System for a rigid satellite . Design
the control Configuration for the give control system as given
follows. (Previous example taken in stability improvement by
state feedback)

Solution:-

The Plant equations are,

                     
                     x(t) = Ax(t) + bu(t)
                     y(t) = cx(t)
 Where
                           0   1              0
                 A                      b                 c     1     0
                           0   0              1
 Here
                     x1(t)= Position   (t )       x2(t)= Position   (t )
Continued…….
The reference i/p    r         r
                                    is a step function. The desired steady-state is,
                                        T
                xs         r        0
As the plant has integrating property, the steady- state value of       u s the i/p
must be zero(otherwise o/p cannot stay constant).

For this case, the shifted regulator problem may be formulated as follows,
                     ~
                     x1        x1           r
                     ~
                     x2            x2
Shifted regulator variables satisfy the equations.
                         
                         ~ = A~ + b~
                         x    x    u
The state – feedback control

                     u(t) = - kx(t)
Continued…….
Therefore ,
                   
                   ~ = (A - bk)~
                   x           x
As in previous example, we found eigenvalues of   (A - bk)are placed at
the desired location - 4    j4 when,

                  k       k1     k2        32      8
The control law expressed in terms of the original state variables is given as,


              u       k1~1 k2 ~2
                        x     x             k1 x1 k2 x2         k1   r

                      kx k1       r
Continued…….
The control configuration for attitude control of the satellite is showing as
following,



          r




                          Attitude Control of a Satellite
State Feedback with Integral Control
Need of state feedback with integral control:

The control configuration of previous problem produces a generalization of
Proportional & Derivative feedback but it dose not include integral control
unless special steps are taken in the design process.

For the system
                             
                             x(t) = Ax(t) + bu(t)
                             y(t) = cx(t)
We can feedback the state “x” as well as the integral of the error in output
by augmenting the plant state “x” with extra “integral state” z,

defined by the equation                 t
                              z(t)          (y(t)- r)dt
                                                           ……….………….…(i)
                                        0
Continued…….
Since z(t) satisfies the differential equation,

              
              z(t)       y(t ) r        cx(t ) r                    ……….………….…(ii)
It is easily included by augmenting the original system as follows:

          
          x         A 0 x                b              0
                                               u               r    ……….………….…(iii)
          
          z          c    0 z            0                 1
Since “r” is constant, in the steady – state   
                                               x         
                                                      0, z         0, provided that the
system is stable.

This means that the steady -state solutions        xs , zs & u s    must satisfy the
equation

              0               A 0 xs                   b
                    r                                       us
                1             c 0 zs                   0             ……….………….…(iv)
Continued…….
Therefore,

From equation (iii) & (iv)

         
         x         A 0 x xs                   b
                                                  (u us )
         
         z         c 0 z zs                   0                ….………….…(v)

Now define new state variables as follows , representing the deviations from
the steady - state:

                               ~    x    xs
                               x
                                    z    zs
                               ~
                               u   (u us )                    ….………….…(vi)
In terms of these variables,
                               
                               ~
                               x   A~
                                    x       ~
                                           bu                 ….………….…(vii)
Continued…….
Where,
                    A     0              b
            A                     b
                    c     0              0
The significance of this result is that by defining the deviation from steady-
state as state & control variables,

The design problem has been reformulated to be the Standard regulator
problem with    ~ 0
                x    as the desired state.

We assume that an asymptotically stable solution to this problem exists & is
given by-

                          u = -k~
                                x
Partitioning “k” appropriately & using eqns. (vi)

                          k     [k p     ki ]
Continued…….
                                          x    xs
         u      us        kp       ki
                                          z    zs
                         kp (x          xs )   ki ( z     zs )
The steady-state terms must balance, therefore
                                                      t
        u        kpx      ki z           kpx        ki ( y (t )   r )dt
                                                      0
The control, thus consist of proportional state feedback & integral control of
output error.

At steady-state,     
                     ~
                     x   o ; therefore
              
          lim z (t )           0    or          lim y(t )         r
            t                                   t
Continued…….
Thus, by integrating action , the output “y” is driven to the no- offset
condition. This will be true even in the presence of constant disturbances
acting on the plant.

                                                 w
             r                          u               y
                         ki
                                                 x
                                        kp



                   State feedback with integral control
Numerical Problem
Design the integral control system with a constant reference
command signal.

Given         Y ( s)           1
                                             with             5    &         0.5
                                                     n
              U ( s)      (s       3)
Solution:-

Characteristic equation will be-                         s2       5s    25   0

Plant equation will be-                                  
                                                         x         3x   u
                                                         y        x
Augmenting the plant state “x” with the integral state “z” defined by the
equation.
                                        t
                          z(t)              (y(t)- r)dt
                                    0
Continued…….

                          
                          x        3 0 x           1       0
We get                                                 u         r
                          
                          z        1       0   z   0        1
Since                     x   xs
                ~
                x
                          z   zs
                ~
                u        (u us )

                                       
                                       ~        3 0 ~      1 ~
State equation becomes                 x            x        u
                                               1 0         0
Continued…….

We can find “k” from


                       3 0               1
      det sI                                 k      s2       5s      25
                       1       0         0

After solving                  s2       (3 k1 ) s       k2      s2       5s   25

Therefore                  k        2    25      [k p        ki ]
                                                                     t
The control                u        k p x ki z          2 x 25 ( y (t ) r )dt
                                                                     0
Continued…….
State feedback with integral control

                                                  w
           r                           1                             y
                        25             s


                                              2


   This system will behave according to the desired closed-loop roots & will
   exhibits the characteristics of integral control:

   Zero steady-state error to a step “r” & zero steady –state error to a
   constant disturbance “w”.
Thank You

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Pole placement by er. sanyam s. saini (me reg)

  • 1. Pole -Placement Design & State Observer Presented by:- Er. Sanyam S. Saini ME(I&C) Regular
  • 2. Outlines • Servo Design: Introduction of the reference Input by Feed forward Control • State Feedback with Integral Control
  • 3. Servo Design: Introduction of the Reference Input by Feed Forward Control  The characteristics Equation of the Closed –Loop Control System is chosen so as to give satisfactory Transient to disturbances.  However, no mention is made of a reference i/p or a design consideration to yield good transient response with respect to command changes. In general, both of these considerations should be taken into account in the designing of control system. This can be done by the proper introduction of the references i/p into the system equations.
  • 4. Continued……. Consider the completely controllable SISO LTI system with nth – order state variable model  x(t) = Ax(t) + bu(t) …………….…………………(i) y(t) = cx(t) …………….…..………….…(ii) We assume that all the n state variables can be accurately measured at all times. Implementation of appropriately designed Control Law of the form. u(t) = - kx(t) Let us now assume that for the system given by equs.(i & ii), the desired steady- state value of the controllable variable y(t) is a constant reference input r. For this servo system, the desired equilibrium state x s is a constant point in state space & is governed by the equations. cx s = r …………….…..………………………………(iii)
  • 5. Continued……. We can formulate this command-following problem as a ”Shifted Regulator Problem”, by shifting the origin of the state space to the equilibrium point x s . 0 = Axs + bu s …………….………..………….…(iv) Assuming for the present that a u s exists that satisfies equns. (iii & iv) us ~(t) = u(t) - u u s ~(t) = x(t) - x x s .………..………….…..(v) ~(t) = y(t) - r y The shifted variables satisfy the equations  ~ = A~ + b~ x x u .………..………….…..(vi) ~ = c~ y x .………..……………...(vii)
  • 6. Continued……. This system possesses a time – invariant asymptotically stable control law ~ = -k~ u x .………..………….…..(viii) In terms of the original state variables , total control effort u(t) -kx(t) us kxs .………..….……….…..(ix) (A - bk)x s b(us kxs ) 0 or xs ( A bk ) 1 b(us kxs ) 1 cx s r c( A bk ) b(us kxs ) The equation has a unique solutions for (us kxs ) ; (u s kx s ) Nr .………..………….…..(x)
  • 7. Continued……. Where N is a scalar feedforword gain, given by N -1 c( A bk ) 1 b The control law (ix), therefore takes the form u(t) - kx(t) Nr w r u y N PLANT + _ x K Control Configuration of a Servo System
  • 8. Numerical Problem Consider a Attitude Control System for a rigid satellite . Design the control Configuration for the give control system as given follows. (Previous example taken in stability improvement by state feedback) Solution:- The Plant equations are,  x(t) = Ax(t) + bu(t) y(t) = cx(t) Where 0 1 0 A b c 1 0 0 0 1 Here x1(t)= Position (t ) x2(t)= Position (t )
  • 9. Continued……. The reference i/p r r is a step function. The desired steady-state is, T xs r 0 As the plant has integrating property, the steady- state value of u s the i/p must be zero(otherwise o/p cannot stay constant). For this case, the shifted regulator problem may be formulated as follows, ~ x1 x1 r ~ x2 x2 Shifted regulator variables satisfy the equations.  ~ = A~ + b~ x x u The state – feedback control u(t) = - kx(t)
  • 10. Continued……. Therefore ,  ~ = (A - bk)~ x x As in previous example, we found eigenvalues of (A - bk)are placed at the desired location - 4 j4 when, k k1 k2 32 8 The control law expressed in terms of the original state variables is given as, u k1~1 k2 ~2 x x k1 x1 k2 x2 k1 r kx k1 r
  • 11. Continued……. The control configuration for attitude control of the satellite is showing as following, r Attitude Control of a Satellite
  • 12. State Feedback with Integral Control Need of state feedback with integral control: The control configuration of previous problem produces a generalization of Proportional & Derivative feedback but it dose not include integral control unless special steps are taken in the design process. For the system  x(t) = Ax(t) + bu(t) y(t) = cx(t) We can feedback the state “x” as well as the integral of the error in output by augmenting the plant state “x” with extra “integral state” z, defined by the equation t z(t) (y(t)- r)dt ……….………….…(i) 0
  • 13. Continued……. Since z(t) satisfies the differential equation,  z(t) y(t ) r cx(t ) r ……….………….…(ii) It is easily included by augmenting the original system as follows:  x A 0 x b 0 u r ……….………….…(iii)  z c 0 z 0 1 Since “r” is constant, in the steady – state  x  0, z 0, provided that the system is stable. This means that the steady -state solutions xs , zs & u s must satisfy the equation 0 A 0 xs b r us 1 c 0 zs 0 ……….………….…(iv)
  • 14. Continued……. Therefore, From equation (iii) & (iv)  x A 0 x xs b (u us )  z c 0 z zs 0 ….………….…(v) Now define new state variables as follows , representing the deviations from the steady - state: ~ x xs x z zs ~ u (u us ) ….………….…(vi) In terms of these variables,  ~ x A~ x ~ bu ….………….…(vii)
  • 15. Continued……. Where, A 0 b A b c 0 0 The significance of this result is that by defining the deviation from steady- state as state & control variables, The design problem has been reformulated to be the Standard regulator problem with ~ 0 x as the desired state. We assume that an asymptotically stable solution to this problem exists & is given by- u = -k~ x Partitioning “k” appropriately & using eqns. (vi) k [k p ki ]
  • 16. Continued……. x xs u us kp ki z zs kp (x xs ) ki ( z zs ) The steady-state terms must balance, therefore t u kpx ki z kpx ki ( y (t ) r )dt 0 The control, thus consist of proportional state feedback & integral control of output error. At steady-state,  ~ x o ; therefore  lim z (t ) 0 or lim y(t ) r t t
  • 17. Continued……. Thus, by integrating action , the output “y” is driven to the no- offset condition. This will be true even in the presence of constant disturbances acting on the plant. w r u y ki x kp State feedback with integral control
  • 18. Numerical Problem Design the integral control system with a constant reference command signal. Given Y ( s) 1 with 5 & 0.5 n U ( s) (s 3) Solution:- Characteristic equation will be- s2 5s 25 0 Plant equation will be-  x 3x u y x Augmenting the plant state “x” with the integral state “z” defined by the equation. t z(t) (y(t)- r)dt 0
  • 19. Continued…….  x 3 0 x 1 0 We get u r  z 1 0 z 0 1 Since x xs ~ x z zs ~ u (u us )  ~ 3 0 ~ 1 ~ State equation becomes x x u 1 0 0
  • 20. Continued……. We can find “k” from 3 0 1 det sI k s2 5s 25 1 0 0 After solving s2 (3 k1 ) s k2 s2 5s 25 Therefore k 2 25 [k p ki ] t The control u k p x ki z 2 x 25 ( y (t ) r )dt 0
  • 21. Continued……. State feedback with integral control w r 1 y 25 s 2 This system will behave according to the desired closed-loop roots & will exhibits the characteristics of integral control: Zero steady-state error to a step “r” & zero steady –state error to a constant disturbance “w”.