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外文翻译--- 火力发电厂先进的蒸汽温度调节控制算法.docx
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外文翻译--- 火力发电厂先进的蒸汽温度调节控制算法.docx
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英文翻译部分
英文部分:
Advanced control algorithms for steam temperature
regulation of thermal power plants
A.Sanchez-Lopez,G.Arroyo-Figueroa*,A.Villavicencio-Ramirez
Instituto de Investigaciones Electricas, Division de Sistemas de Control, Reforma No.
113, Colonia Palmira,Cuernavaca, Morelos 62490, Mexico
Received 5 February 2003; revised 6 April 2004; accepted 8 July 2004
Abstract
A model-based controller (Dynamic Matrix Control) and an intelligent controller
(Fuzzy Logic Control) have been designed and implemented for steam temperature
regulation of a 300 MW thermal power plant. The temperature regulation is
considered the most demanded control loop in the steam generation process. Both
proposed controllers Dynamic Matrix Controller (DMC) and Fuzzy Logic Controller
(FLC) were applied to regulate superheated and reheated steam temperature. The
results show that the FLC controller has a better performance than advanced model-
based controller, such as DMC or a conventional PID controller. The main benefits
are the reduction of the overshoot and the tighter regulation of the steam temperatures.
FLC controllers can achieve good result for complex nonlinear processes with
dynamic variation or with long delay times.
Keywords: Thermal power plants; Power plant control; Steam temperature
regulation; Predictive control; Fuzzy logic control
1. Introduction
Current economic and environment factors put a stringer requirement on thermal
power plants to be operated at a high level of efficiency and safety at minimum cost.
In addition, there are an increment of the age of thermal plants that affected the
reliability and performance of the plants. These factors have increased the complexity
of power control systems operations [1,2].
Currently, the computer and information technology have been extensively used
in thermal plant process operation and control. Distributed control systems (DCS) and
management information systems (MIS) have been playing an important role to show
![](https://csdnimg.cn/release/download_crawler_static/85495811/bg2.jpg)
the plant status. The main function of DCS is to handle normal disturbances and
maintain key process parameters in pre-specified local optimal levels. Despite their
great success, DCS have little function for abnormal and non-routine operation
because the classical proportional-integral-derivative (PID) controlis widely used by
the DCS. PID controllers exhibit poor performance when applied to process
containing unknown non-linearity and time delays. The complexity of these problems
and the difficulties in implementing conventional controllers to eliminate variations in
PID tuning motivate the use of other kind of controllers, such as model-based
controllers and intelligent controllers.
This paper proposes a model-based controller such as Dynamic Matrix
Controller (DMC) and an intelligent controller based on fuzzy logic as an alternative
control strategy applied to regulate the steam temperature of the thermal power plant.
The temperature regulation is considered the most demanded control loop in the steam
generation process. The steam temperature deviation must be kept within a tight
variation rank in order to assure safe operation, improve efficiency and increase the
life span of the equipment. Moreover, there are many mutual interactions between
steam temperature control loops that have been considered. Other important factor is
the time delay. It is well know that the time delay makes the temperature loops hard to
tune. The complexity of these problems and difficulties to implement PID
conventional controllers motivate to research the use of model predictive
controllerssuch as the DMC or intelligent control techniques such as the Fuzzy Logic
Controller (FLC) as a solution for controlling systems in which time delays, and non-
linear behavior need to be addressed [3,4]. The paper is organized as follows. A brief
description of the DMC is presented in Section 2. The FLC design is described in
Section 3. Section 4 presents the implementation of both controllers DMC and FLC to
regulate the superheated and reheated steam temperature of a thermal power plant.
The performance of the FLC controller was evaluated against two other controllers,
the conventional PID controller and the predictive DMC controller. Results are
presented in Section 5. Finally, the main set of conclusions according to the analysis
and results derived from the performance of controllers is presented in Section 6.
2. Dynamic matrix control
The DMC is a kind of model-based predictive control (Fig. 1). This controller
was developed to improve control of oil refinement processes [5]. The DMC and
other predictive control techniques such as the Generalized Predictive Control [6] or
Smith predictor [6] algorithms are based on past and present information of controlled
and manipulated variables to predict the future state of the process.
The DMC is based on a time domain model. This model is utilized to predict the
future behavior of the process in a defined time horizon (Fig. 2). Based on this precept
the control algorithm provides a way to define the process behavior in the time,
predicting the controlled variables trajectory in function of previous control actions
and current values of the process [7]. Controlled behavior can be obtained calculating
the suitable future control actions. To obtain the process model, the system is
![](https://csdnimg.cn/release/download_crawler_static/85495811/bg3.jpg)
perturbed with an unitary step signal as an input disturbance (Fig. 3).
This method is the most common and easy mean to obtain the dynamic matrix
coefficients of the process. The control technique includes the followings procedures:
(a) Obtaining the Dynamic Matrix model of the process. In this stage, a step
signal is applied to the input of the process. The measurements obtained with this
activity represent the process behavior as well as the coefficients of the process state
in time. This step is performed just once before the operation of the control algorithm
![](https://csdnimg.cn/release/download_crawler_static/85495811/bg4.jpg)
in the process.
(b) Determination of deviations in controlled variables. In this step, the deviation
between the controlled variables of the process and their respective set points is
measured.
(c) Projection of future states of the process. The future behavior of each
controlled variable is defined ina vector. This vector is based on previous control
actions and current values of the process.
(d) Calculation of control movements. Control movements are obtained using the
future vector of error and the dynamic matrix of the process. The equation developed
to obtain the control movements is shown below:
where A represents the dynamic matrix, AT the transpose matrix of A X the
vector of future states of the process, f a weighting factor, I the image matrix and D he
future control actions. Further details about this equation are found in Ref. [5].
(e) Control movements’ implementation. In this step the first element of the
control movements’ vector is applied to manipulated variables. A DMC controller
![](https://csdnimg.cn/release/download_crawler_static/85495811/bg5.jpg)
allows designers the use of time domain information to create a process model. The
mathematical method for prediction matches the predicted behavior and the actual
behavior of the process to predict the next state of the process. However, the process
model is not continuously updated because this involves recalculations that can lead
to an overload of processors and performance degradation.Discrepancies in the real
behavior of the process and the predicted state are considered only in the current
calculation of control movements. Thus, the controller is adjusted continuously based
on deviations of the predicted and real behavior while the model remains static.
3. Fuzzy logic control
Fuzzy control is used when the process follows some general operating
characteristic and a detailed process understanding is unknown or process model
become overly complex. The capability to qualitatively capture the attributes of a
control system based on observable phenomena and the capability to model the
nonlinearities for the process are the main features of fuzzy control. The ability of
Fuzzy Logic to capture system dynamics qualitatively and execute this qualitative
schema in a real time situation is an attractive feature for temperature control systems
[8]. The essential part of the FLC is a set of linguistic control rules related to the dual
concepts of fuzzy implication and the compositional rule of inference [9].
Essentially, the fuzzy controller provides an algorithm that can convert the
linguistic control strategy, based on expert knowledge, into an automatic control
strategy. In general, the basic configuration of a fuzzy controller has five main
modules as it is shown in Fig. 4.
In the first module, a quantization module converts to discrete values and
normalizes the universe of discourse of
various manipulated variables (Input). Then, a numerical fuzzy converter maps
crisp data to fuzzy numbers characterized by a fuzzy set and a linguistic label
(Fuzzification). In the next module, the inference engine applies the compositional
rule of inference to the rule base in order to derive fuzzy values of the control signal
from the input facts of the controller. Finally, a symbolic-numerical interface known
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