Environmental Engineering Reference
In-Depth Information
Combining equations (3.8), (3.9) and (3.10), the realisation of the generalised plant is then
obtained as
A
0
0
B 1
B 2
B w ξ
B w C 1
A w
B w D 1
B w D 2
P
=
0
C w
0
0
0
.
(3.11)
μ
-----------------------------------------------
C 1
0
0
0
0
0
ξ
D 1
D 2
The stabilising controller C can be calculated using the results on H controller design (Zhou
et al. 1996) for the generalised plant P .
3.2.3 Evaluation of the System Stability
According to (Weiss and Hafele 1999; Weiss et al. 2004), the closed-loop system in Figure 3.2 is
exponentially stable if the closed-loop system from Figure 3.4 is stable and its transfer function
from a to b , denoted T ba , satisfies
T ba <
1. Assume that the state-space realisation of the
controller is
A c B c
C c D c
C
=
.
(3.12)
Note that the controller obtained from the H design is always strictly proper. However, after
controller reduction, the reduced controller may not be strictly proper. The realisation of the
transfer function from a to b , assuming that
w =
0 and noting that D 2 =
0, can be found as
follows:
1
A B 2
C 1 D 2
C 1
T ba =
W
1
A
A c B c
C c D c
1 A w
B 2
B w
=
C 1
0
C w
0
.
A
+
B 2 D c C 1 B 2 C c B 2 D c C w
0
B c C 1
A c
B c C w
0
=
0
0
A w
B w
C 1
0
C w
0
Once the controller C is obtained, the stability of the system can be verified by checking
T ba . The realisation of the transfer function from
w
to e , assuming that
v =
0, can be
 
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