1) integrating and unstable plant
积分和不稳定对象
1.
Robust control method for integrating and unstable plants with time delay;
具有时滞的积分和不稳定对象的鲁棒控制
2) unstable plant
不稳定对象
1.
PID control of unstable plants;
不稳定对象的PID控制
2.
The results indicate that the H_∞output feedback design of such a non-minimum-phase unstable plant is far less robust.
针对倒立摆输出反馈的鲁棒性问题,采用H∞的两块和四块问题进行系统性的优化设计,设计结果表明,这类非最小相位不稳定对象的H∞输出反馈设计缺乏鲁棒性。
3) unstable process
不稳定对象
1.
Based on the H ∞ frequency domain optimal control theory PID controllers were designed for open loop unstable processes with time delay.
针对典型不稳定对象推导了 PID控制器整定公式 。
2.
The simulation results show that the proposed analytical controller design scheme achieves shorter rise-time and smaller over-shoot, better dynamic performance and robustness is also provided for the first order unstable processes with large dead time.
针对工业过程控制中一类常见的一阶大时滞不稳定对象不易控制的问题,本文首先采用内模控制和控制器参数化原理,提出一种简单PID控制器的解析设计方法。
4) unstable plus time delay processes
不稳定滞后对象
1.
Predictive PID control for several kinds of unstable plus time delay processes;
几种不稳定滞后对象的预测PID控制
5) unstable FOPDT plant
一阶时滞不稳定对象
1.
Multi-objective optimization of PID controller parameters for unstable FOPDT plants;
一阶时滞不稳定对象的PID控制器多目标优化设计
6) integrating process
积分对象
1.
On the basis of impulse response of the integrating processes, a predictive functional control algorithm was proposed, and a load rejection controller was designed by optimal control theory so that the desinged control system can track setpoint without steady state error in the presence of input disturbance.
所提算法能同时适用于反向响应积分对象和大时间滞后积分对象的控制。
2.
A predictive functional control algorithm based on impulse response model is designed for integrating processes in this paper.
基于积分对象脉冲响应设计预测函数控制器,引入一种新的误差反馈校正方法可有效消除系统稳态误差。
补充资料：稳定极限和静态稳定储备系数
稳定极限和静态稳定储备系数
stability limit and steady state stability margin
wend一ngJ一xlorl heJ一r飞gt。}咖erld一rlgc}〕LJ匕fJ稳定极限和静态稳定储备系数x}S)〕走』limit and steady一state stability margin)力系统德定。(stability 见电
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条