IMC based Smith Predictor Design with PI+CI Structure: Control of Delayed MIMO Systems
MATEC Web of Conferences 4 2 , 0 1 0 1 1 (2016 )
DOI: 10.1051/ m atecconf/ 2016 4 2 0 1 0 1 1
C Owned by the authors, published by EDP Sciences, 2016
IMC based Smith Predictor Design with PI+CI Structure:
Control of Delayed MIMO Systems
1,a
2
3
Ali Dokht Shakibjoo , Nastaran Vasegh and Hassan HosseinNia
1, 2
3
Departement of Electrical Engineering, Shahid Rajaee Teacher Training university, Tehran, Iran
Departement of Precision and Microsystems Engineering, Delft University of Technology, The Netherlands
Abstract. In this study a novel structure for time-delay MIMO systems controller design is introduced. In this method
decoupled Smith predictor (SP) controller is designed using Internal Model Control structure (IMC). In order to
approximate decoupled system, step response model approximation is employed and simulated on MIMO multiple
time-delay system. Moreover, to improve system performance from overshoot and rise time perspective, Smith
predictor controller is combined with PI+CI structure. Furthermore, to increase system robustness, a low pass filter is
designed. Afterwards, the proposed structure is applied to the model of a time-delay MIMO distillation tower system
and obtained results are compared to those of a PID controller. Finally, performance of different design methods is
evaluated using Integral error criterion (Integral Square Error criterion).
1 Introduction
Time delay is common in most of industrial processes. It
basically results from information, mass and energy
transfer phenomena which are known as groups of time
delays in simple connected dynamic systems. Probing the
impacts of disturbance is time consuming; thus, processes
with significant time delay are difficult to be controlled
by standard feedback controllers. A considerable amount
of recent research works have focused on time delay as it
is the most crucial factor affecting control quality. The
first instance of time-delay compensator for classic
control systems was introduced by Smith in 1957 called
Smith predictor. Smith predictor aims to remove time
delay from control loop. As a result a time-delay free
section is achieved for which an ideal controller can be
designed [1,2].
The PI+CI controller consists of two parallel PI and
CI controllers [3]. Clegg Integral (CI) is the simplest
structure for reset control which increases the phase of
system and its stability. Reset action occurs when the
input signal is set to zero. Additionally, CI is able to
overcome limitations of LTI control system. It was firstly
introduced by Clegg in 1985 [4]. To design PI+CI
structure PI controller is designed in first step so that the
most speed and overshoot could be achieved. Then,
nonlinear reset mechanism is added to reduce overshoot.
Changing reset coefficient which is between [0, 1], the
best output, from performance indices perspective, might
be derived. To date, most of the processes which have
a
been studied using Smith predictor were single input
single output systems. Recently, PI+CI structure with
Smith predictor control is designed for time-delay first
order system [5]. However, this method is not simulated
for MIMO systems. In this paper, Smith predictor
controller is designed using internal model control
structure. This structure is applied to a distillation tower
system. To improve output response PI+CI controller is
added. Finally, comparing simulation results to PID
controller, the potential of this hybrid structure for
improving performance indices of MIMO systems is
discovered.
After PI+CI structure and Smith predictor controller
are introduced, the Smith predictor controller with
Internal Model Control is designed in section 3.
Afterwards, adjustment of PI+CI structure is discussed to
improve system performance. Then, this structure is
applied to a MIMO distillation tower system model. Also,
results of desired system are compared to PID controller.
At the end, the results are validated using Integral error
criterion (Integral Square Error criterion). The final
section concludes the paper.
2 Equivalent structure for Smith
predictor controller with Internal Model
Control
In this study an equivalent structure of Internal Model
Control together with a Smith predictor compensator are
utilized. The structure is depicted in figure 1.
Corresponding author:
This is an Open Access article distributed under the terms of the Creative Commons Attribution License 4.0, which permits
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Article available at http://www.matec-conferences.org or http://dx.doi.org/10.1051/matecconf/20164201011
MATEC Web of Conferences
g1m ( s )
g 2m ( s )
g mm ( s )
g 11( s ) g12 ( s )
g ( s ) g 22 ( s )
G( s ) 21
g (s) g (s)
m2
m1
According to the structure demonstrated in figure 1,
Gnc ( s ) is Internal Model controller, Gc ( s ) is Smith
predictor controller, G( s ) is the actual system, Gm ( s ) is
system model, Gm0 ( s ) is the system model ignoring time
Figure 1. Controller scheme
It is a combination of both Internal Model Control
structure (figure 2) and Smith predictor structure (figure 3)
and takes advantage of these two structures
simultaneously.
delay and GF ( s ) is the filter. Initially, using the
structure of Internal Model control Gnc ( s ) is designed.
Subsequently, Smith predictor controller is derived from
Internal Model Controller. Considering figure 1 we have:
Gnc ( s )
Gc ( s )
1 Gc ( s )G( s )
And consequently one may write:
Gc ( s )
Gnc ( s )
1 Gnc ( s )G( s )
To adjust parameters of Gc ( s ) controller, a first order
time-delay system is assumed as follows:
Figure 2. MIC scheme
Ĝ( s )
Kes
Ts 1
It could be separated as shown below:
Ĝ( s ) Ĝ ( s )Ĝ ( s ) Ĝ ( s ) e s Ĝ ( s )
Figure 3. Smith predictor scheme
In the Internal Model Control structure disadvantages
such as open loop system, sensitivity to modelling errors
and lack of disturbance rejection ability are eliminated. In
case of perfect matching between model and process, as
well as no disturbance, the system operates as an open
loop system which may achieve precise and rapid
tracking; whereas, in presence of either mismatch
between model and process, or disturbance entrance into
the system, it operates as a closed loop system which is
able to remove disturbance effects. In our research, the
system is a time-delay one; therefore, equivalent structure
of Smith predictor together with Internal Model
Controller are exploited [6, 7].
K
Ts 1
Ĝ ( s ) Includes all time delays and right half plane
zeros. Modelling errors must be minimized in internal
model controller. Notice that difference between model
and process behaviour happens in high frequencies at the
end of frequency response. Hence, a series low pass filter
is utilized with Internal Model Controller to attenuate
mismatch impact. F ( s ) is the simplest type of low pass
fi (...truncated)