1999
DOI: 10.1016/s0967-0661(98)00166-x
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Robust identification of first-order plus dead-time model from step response

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Cited by 142 publications
(79 citation statements)
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“…The model of the discharge flow, (wherev 1 and q 1 are input variable and output variable, respectively) and the model of the steam flow, (wherev 2 and q 2 are input variable and output variable, respectively) can be constructed using the process data. The dynamics of the above two valves can be described by the first-order plus dead-time models form as follows [16], [17]:…”
Section: B Dynamic Modeling Of the Control Valvementioning
confidence: 99%
“…The model of the discharge flow, (wherev 1 and q 1 are input variable and output variable, respectively) and the model of the steam flow, (wherev 2 and q 2 are input variable and output variable, respectively) can be constructed using the process data. The dynamics of the above two valves can be described by the first-order plus dead-time models form as follows [16], [17]:…”
Section: B Dynamic Modeling Of the Control Valvementioning
confidence: 99%
“…It is made by measuring the system step response and by using a least square type algorithm to approximate the process with a first-order plus dead-time model (see (Bi et al 1999)). For steps having amplitude of (1, 2 and 3), the identified continuous-time pole is (1.99×10 −3 , 2.33×10 −3 and 2.5×10 −3 ), which justifies the choice of 0.99 for the Laguerre basis pole.…”
Section: Multiple Models System Identificationmentioning
confidence: 99%
“…Identification of FOPDT or SOPDT models from process empirical data helps in representing complex processes in minimum parameters and simple model structure but holding the essential process dynamics without the need of knowing the complex physics involved in the process. The simplest and easiest method for FOPDT or SOPDT model parameter estimation from empirical data is by the open-loop step test of the process [7][8][9].…”
Section: Introductionmentioning
confidence: 99%