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7/29/2019 Control Theory - Control-Intro PPT
1/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Open Loop
Plant Characteristics
Linearity
Linear or State variable repr.
State variable repr.
Transfer Function (observable & controllable part): Y(s)/U(s)
Non Linear
State Variable repr.
Linear Approximation (Linerarization at operational points,
Describing Function, etc)
PlantU(t) Y(t)
X AX BU Y CX DU= + = +
( , ) ( , )X f X U Y g X U= =
7/29/2019 Control Theory - Control-Intro PPT
2/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Time
Time Invariance (fixed coefficients)
Time Variance (dynamic coefficients)
Granularity
lumped parameters (linear differential equations) distributed parameters (partial differential equations)
Number of Inputs and Outputs
SISO, SIMO, MISO, MIMO
( ( ), ( ), ) ( ( ), ( ), )X f X t U t t Y g X t U t t= =
7/29/2019 Control Theory - Control-Intro PPT
3/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Closed Loop (Output feedback)
Bang-Bang Control
E = SP - YU = Sign(E) orU = Sign(E+/- 1/2gap)
gap
Issues:
Limit Cycles and Overshooting
Gap reduces cycling frequency
PlantU(t) Y(t)ControllerSP+
-
E
E
U
7/29/2019 Control Theory - Control-Intro PPT
4/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Closed Loop (Output feedback)
Proportional Control
KP = Proportional Gain (to control rise time)
M = Manual reset
Issues: Offset Error (SSE)
E = SP - Y
U K E M P= +
PlantU(t) Y(t)ControllerSP+
-
E
E
M
UKP
1
7/29/2019 Control Theory - Control-Intro PPT
5/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Closed Loop (Output feedback)
Proportional Integral (PI) Control
E = SP - YEdtKEKU IP +=
KP = Proportional Gain (to control rise time)KI = Integral Gain (to control SSE)
M = Manual reset
Issues: Slow in correcting SSE
PlantU(t) Y(t)ControllerSP+
-
E
E
U
E ControlSurface
7/29/2019 Control Theory - Control-Intro PPT
6/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
Closed Loop (Output feedback)
PlantU(t) Y(t)ControllerSP+
-
E
Proportional Integral Derivative (PID) Control
E = SP - Y
dt
dEKEdtKEKU DIP ++=
KP = Proportional Gain (to control rise time)KI = Integral Gain (to control SSE)
KD = Derivate Gain (to anticipate error)
Issues: Pure Derivative term not realizable (non-causal)
7/29/2019 Control Theory - Control-Intro PPT
7/7
Copyright 1998, Dr. Piero P. Bonissone, All Rights Reserved
Control Theor
dt
dEKEdtKEKU DIP ++=
Issues: Pure Derivative term not realizable (non-causal)
Usually solved by placing a pole with large negative value (-A):
U s
E sK
T sT s
KT s
Ts
s A
I
D
I
D
( )
( )( )
( )
= + +
+ ++
11
11