Proceedings of the 1998 IEEE International Conference on Control Applications (Cat. No.98CH36104)
DOI: 10.1109/cca.1998.721628
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Adaptive control for the steam temperature of thermal power plants

Abstract: Excellent control, minimal error from setpoint, of a boiler unit has always been an elusive goal. Adap tive Control System was applied to steam temperature control of utility boilers. In the control system, the adaptive control strategy is embedded on the DCS controllers in parallel with each conventional

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Cited by 22 publications
(10 citation statements)
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“…[8][9][10]. Denote the estimate of variable y byŷ, definitions of the mean absolute error, standard deviation of the absolute errors, mean relative error and standard deviation of the relative errors are given in Table 1.…”
Section: Nonlinear Regression Modelingmentioning
confidence: 99%
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“…[8][9][10]. Denote the estimate of variable y byŷ, definitions of the mean absolute error, standard deviation of the absolute errors, mean relative error and standard deviation of the relative errors are given in Table 1.…”
Section: Nonlinear Regression Modelingmentioning
confidence: 99%
“…Although some energy-intrusive techniques, such as tunable diode laser absorption spectroscopy [2,3], laser induced breakdown spectroscopy [4] and X-ray fluorescence analysis [5], have been used to measure some interested parameters including temperature, gas concentration, etc., from attenuation or spectral variation of the penetrated rays in engine design, http://dx.doi.org/10.1016/j.fuel.2014. 10.081 0016-2361/Ó 2014 Elsevier Ltd. All rights reserved. the techniques have limited applications in design and monitoring of large scale industrial boilers due to complicated industrial environments.…”
Section: Introductionmentioning
confidence: 96%
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“…The prior study is the literature [1] which extends a general furnace follow machine method according to the compensator based on state feedback, aimed to reduce the coupling influence among the systems. Paper [2] designs a feedback controller to achieve the in-connected controlling between the steam pressure of the evaporator export and the enthalpy value.Subsequently, the self-adaptive control theory is applied in the steam temperature [3] . In this paper, the control value is the sum of the weighted variables and the weighted variables are self-adaptive control value and the classical control value, and they are exist simultaneity.…”
mentioning
confidence: 99%
“…Subsequently, the self-adaptive control theory is applied in the steam temperature [3] . In this paper, the control value is the sum of the weighted variables and the weighted variables are self-adaptive control value and the classical control value, and they are exist simultaneity.…”
mentioning
confidence: 99%