工艺设备控制中二阶加死区时间系统的高效参数估计

Mahua Pal, Kumardeb Banerjee, Bivas Dam
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Two-time domain performance indices (PIs), <span></span><math>\n <mrow>\n <msub>\n <mi>T</mi>\n <mi>R</mi>\n </msub>\n </mrow></math> (= <span></span><math>\n <mrow>\n <mfrac>\n <msub>\n <mi>t</mi>\n <mn>90</mn>\n </msub>\n <msub>\n <mi>t</mi>\n <mn>10</mn>\n </msub>\n </mfrac>\n </mrow></math> for system dead time = 0 and <span></span><math>\n <mrow>\n <mfrac>\n <mrow>\n <msub>\n <mi>t</mi>\n <mn>90</mn>\n </msub>\n <mo>−</mo>\n <msub>\n <mi>t</mi>\n <mn>5</mn>\n </msub>\n <mspace></mspace>\n </mrow>\n <mrow>\n <msub>\n <mi>t</mi>\n <mn>10</mn>\n </msub>\n <mo>−</mo>\n <msub>\n <mi>t</mi>\n <mn>5</mn>\n </msub>\n <mspace></mspace>\n </mrow>\n </mfrac>\n </mrow></math> for system dead time ≠ 0; <span></span><math>\n <mrow>\n <msub>\n <mi>t</mi>\n <mn>5</mn>\n </msub>\n </mrow></math>, <span></span><math>\n <mrow>\n <msub>\n <mi>t</mi>\n <mn>10</mn>\n </msub>\n </mrow></math> and <span></span><math>\n <mrow>\n <msub>\n <mi>t</mi>\n <mn>90</mn>\n </msub>\n </mrow></math> are respectively the times at which the response reaches 5%, 10% and 90% of the steady-state response) and <span></span><math>\n <mrow>\n <msub>\n <mi>f</mi>\n <mi>r</mi>\n </msub>\n </mrow></math> (reciprocal of rise time <span></span><math>\n <mrow>\n <msub>\n <mi>t</mi>\n <mi>r</mi>\n </msub>\n </mrow></math>) are proposed in this work. Correlations are established between these PIs and the parameters of the SOPDT system. The first correlation establishes that <span></span><math>\n <mrow>\n <msub>\n <mi>T</mi>\n <mi>R</mi>\n </msub>\n </mrow></math> is a function of the damping ratio <span></span><math>\n <mrow>\n <mi>ξ</mi>\n </mrow></math> only and is independent of the undamped natural frequency <span></span><math>\n <mrow>\n <mspace></mspace>\n <msub>\n <mi>ω</mi>\n <mi>n</mi>\n </msub>\n <mo>,</mo>\n </mrow></math> which means that the evaluation of <span></span><math>\n <mrow>\n <msub>\n <mi>T</mi>\n <mi>R</mi>\n </msub>\n </mrow></math> from the time response data is sufficient to estimate <span></span><math>\n <mrow>\n <mi>ξ</mi>\n </mrow></math>. The second correlation establishes that for a given <span></span><math>\n <mrow>\n <mi>ξ</mi>\n </mrow></math>, <span></span><math>\n <mrow>\n <msub>\n <mi>f</mi>\n <mi>r</mi>\n </msub>\n </mrow></math> is a function of <span></span><math>\n <mrow>\n <msub>\n <mi>ω</mi>\n <mi>n</mi>\n </msub>\n </mrow></math>. Thus the evaluation of <span></span><math>\n <mrow>\n <msub>\n <mi>f</mi>\n <mi>r</mi>\n </msub>\n </mrow></math> from the time response data and an estimate of <span></span><math>\n <mrow>\n <mi>ξ</mi>\n </mrow></math> from the first correlation is sufficient to estimate <span></span><math>\n <mrow>\n <msub>\n <mi>ω</mi>\n <mi>n</mi>\n </msub>\n </mrow></math>. The proposed algorithm estimates the parameters of the canonical transfer function of the plant by these correlations from the three specific time instants, as mentioned above, of the step response of the plant. 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Since many process plants are characterized as second-order plus dead time (SOPDT) overdamped or critically damped systems, this study presents a straightforward parameter estimation method using transient response data from a step input at three specific time instants. Two-time domain performance indices (PIs), <span></span><math>\\n <mrow>\\n <msub>\\n <mi>T</mi>\\n <mi>R</mi>\\n </msub>\\n </mrow></math> (= <span></span><math>\\n <mrow>\\n <mfrac>\\n <msub>\\n <mi>t</mi>\\n <mn>90</mn>\\n </msub>\\n <msub>\\n <mi>t</mi>\\n <mn>10</mn>\\n </msub>\\n </mfrac>\\n </mrow></math> for system dead time = 0 and <span></span><math>\\n <mrow>\\n <mfrac>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mn>90</mn>\\n </msub>\\n <mo>−</mo>\\n <msub>\\n <mi>t</mi>\\n <mn>5</mn>\\n </msub>\\n <mspace></mspace>\\n </mrow>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mn>10</mn>\\n </msub>\\n <mo>−</mo>\\n <msub>\\n <mi>t</mi>\\n <mn>5</mn>\\n </msub>\\n <mspace></mspace>\\n </mrow>\\n </mfrac>\\n </mrow></math> for system dead time ≠ 0; <span></span><math>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mn>5</mn>\\n </msub>\\n </mrow></math>, <span></span><math>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mn>10</mn>\\n </msub>\\n </mrow></math> and <span></span><math>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mn>90</mn>\\n </msub>\\n </mrow></math> are respectively the times at which the response reaches 5%, 10% and 90% of the steady-state response) and <span></span><math>\\n <mrow>\\n <msub>\\n <mi>f</mi>\\n <mi>r</mi>\\n </msub>\\n </mrow></math> (reciprocal of rise time <span></span><math>\\n <mrow>\\n <msub>\\n <mi>t</mi>\\n <mi>r</mi>\\n </msub>\\n </mrow></math>) are proposed in this work. 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引用次数: 0

摘要

为通常建模为一阶或二阶带死区时间系统的工艺设备设计控制器时,需要对其参数进行有效而准确的估算。由于许多工艺设备都具有二阶加死区时间 (SOPDT) 过阻尼或临界阻尼系统的特征,因此本研究提出了一种直接的参数估计方法,该方法使用三个特定时间时刻的阶跃输入瞬态响应数据。本研究提出了两个时域性能指数(PIs):(= 系统死区时间 = 0 时和系统死区时间≠0 时; 和 分别是响应达到稳态响应 5%、10% 和 90% 的时间)和(上升时间的倒数)。这些 PI 与 SOPDT 系统参数之间建立了相关性。第一种相关性表明,PI 仅是阻尼比的函数,与无阻尼固有频率无关,这意味着从时间响应数据中评估 PI 就足以估算出 SOPDT 系统的......。第二个相关性表明,对于给定的 , , 是 。 因此,根据时间响应数据和第一个相关性的估算值就足以估算出 。拟议算法通过上述三个特定时间瞬时的阶跃响应,利用这些相关性估算出工厂的典型传递函数参数。与文献中已有的四种方法进行比较后发现,该方法对可以用 SOPDT 动力学近似的高阶系统也很有效,而且即使有测量噪声也很稳健,因此不仅适用于工艺设备,也适用于具有类似时间响应的其他系统,有助于实施控制策略。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Efficient parameter estimation for second order plus dead time systems in process plant control

Efficient parameter estimation for second order plus dead time systems in process plant control

Designing a controller for a process plant typically modeled as a first or second-order system with dead time involves an efficient and accurate estimation of its parameters. Since many process plants are characterized as second-order plus dead time (SOPDT) overdamped or critically damped systems, this study presents a straightforward parameter estimation method using transient response data from a step input at three specific time instants. Two-time domain performance indices (PIs), T R (= t 90 t 10 for system dead time = 0 and t 90 t 5 t 10 t 5 for system dead time ≠ 0; t 5 , t 10 and t 90 are respectively the times at which the response reaches 5%, 10% and 90% of the steady-state response) and f r (reciprocal of rise time t r ) are proposed in this work. Correlations are established between these PIs and the parameters of the SOPDT system. The first correlation establishes that T R is a function of the damping ratio ξ only and is independent of the undamped natural frequency ω n , which means that the evaluation of T R from the time response data is sufficient to estimate ξ . The second correlation establishes that for a given ξ , f r is a function of ω n . Thus the evaluation of f r from the time response data and an estimate of ξ from the first correlation is sufficient to estimate ω n . The proposed algorithm estimates the parameters of the canonical transfer function of the plant by these correlations from the three specific time instants, as mentioned above, of the step response of the plant. Comparisons with four methods existing in the literature reveal that the method is also effective with higher order systems that may be approximated by SOPDT dynamics, and robust even with measurement noise, making it useful for implementing control strategies, not only in process plants but also in other systems having similar time responses.

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