INTERNAL MODEL CONTROL .4. PID CONTROLLER-DESIGN

INTERNAL MODEL CONTROL .4. PID CONTROLLER-DESIGN
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DOI:
10.1021/i200032a041
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发表时间:
1986-01-01
期刊:
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT
影响因子:
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通讯作者:
SKOGESTAD, S
SKOGESTAD, S
中科院分区:
其他
文献类型:
--
作者:
RIVERA, DE;MORARI, M;SKOGESTAD, S

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对于流程工业中通常使用的大量单输入单输出(SISO)模型,内模控制(IMC)设计过程被证明导致了PID控制器,有时会增加一阶滞后。这些PID控制器的唯一调整参数是闭环系统的时间常数,或者相当于闭环系统的带宽。因此,在线调整比一般的PID控制器简单得多。作为一种特例,解析地推导了一阶纯滞后时滞系统的PI和PID整定规则。证明了这些规则在闭环系统性能和鲁棒性方面的优越性。
For a large number of single input-single output (SISO) models typically used In the process industries, the Internal Model Control (IMC) design procedure Is shown to lead to PID controllers, occasionally augmented with a first-order lag. ThesePID controllers have as their only tuning parameter the closed-loop time constant or, equivalently, the closed-loop bandwidth. On-line adjustments are therefore much simpler than for general PID controllers. As a special case, PI-and PID-tuning rules for systems modeled by a first-order lag with dead time are derived analytically. The superiority of these rules In terms of both closed-loop performance and robustness is demonstrated.