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Automation Drum-boiler dynamics
Automatica 36 (2000) 363}378
Drum-boiler dynamicsq
K.J. As stroK m!,*, R.D. Bell
!Department of Automatic Control, Lund Institute of Technology, Box 118, S-221 00 Lund, Sweden
Department of Computing, School of Mathematics, Physics, Computing and Electronics, Macquarie University, New South Wales 2109, Australia
Received 2 October 1998; revised 7 March 1999; received in nal form 8 June 1999
Abstract
A nonlinear dynamic model for natural circulation drum-boilers is presented. The model describes the complicated dynamics of the
drum, downcomer, and riser components. It is derived from rst principles, and is characterized by a few physical parameters.
A strong e!ort has been made to strike a balance between delity and simplicity. Results from validation of the model against unique
plant data are presented. The model describes the behavior of the system over a wide operating range. ( 2000 Elsevier Science Ltd.
All rights reserved.
1. Introduction
There are dramatic changes in the power industry
because of deregulation. One consequence of this is that
the demands for rapid changes in power generation is
increasing. This leads to more stringent requirements on
the control systems for the processes. It is required to
keep the processes operating well for large changes in the
operating conditions. One way to achieve this is to incor-
porate more process knowledge into the systems. There
has also been a signicant development of methods for
model-based control, see Garcia, Prett and Morari
(1989), Qin and Badgwell (1997) and Mayne, Rawlings
and Rao (1999). Lack of good nonlinear process models
is a bottleneck for using model-based controllers. For
many industrial processes there are good static models
used for process design and steady-state operation. By
using system identication techniques it is possible to
obtain black box models of reasonable complexity that
describe the system well in specic operating conditions.
Neither static models nor black box models are suitable
fo
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