• CPU 执行指令的基本过程 • 硬连线控制器与微程序控制器 • 微型计算机的特点与分类

设计了基于数字信号处理器(DSP)的热连轧自动厚度控制(AGC)实时仿真器,建立了调厚过程压下系统和变形区的动态模型．仿真时,仿真器实时并行地计算带钢和轧机的模型,计算机控制系统的控制器运行AGC软件,两者通过内存映像网实时交换数据,通过虚拟的对象实现了对AGC软件的实时离线调试．

1 4.1 Traditional Design Methods 2 4.2 H∞ PID Controllers for the First-Order Plant 3 4.3 H∞ PID controller and the Smith Predictor 4 4.4 Quantitative Performance and Robustness 5 4.5 H∞ PID Controllers for the Second-Order Plant 6 4.6 All Stabilizing PID Controllers for Stable Plants

1 3.1 Norms and System Gains 2 3.2 Internal Stability and Performance 3 3.3 Controller Parameterization 4 3.4 Robust Stability and Robust Performance 5 3.5 Robustness of Systems with Time Delays

1 2.1 Process Dynamic Responses 2 2.2 Rational Approximations for Time Delay 3 2.3 Time Domain Performance Indices 4 2.4 Frequency Response Analysis 5 2.5 Transformation of Two Commonly Used Models 6 2.6 Design Requirements and Method Comparison

1 1.1 A Brief History of Control Theory 2 1.2 Design of Feedback Control Systems 3 1.3 Consideration on Control System Design 4 1.4 What This Book is About 5 References for Reading

为了在地下矿生产计划编制过程中控制矿石质量,本文给出了两个能适应不同要求的线性规划模型,介绍了模型的构造及求解方法。模型已经在微型计算机上实现,并应用于西石门铁矿的计划编制工作中

设计了基于数字信号处理器DSP的热连轧自动厚度控制(AGC)实时仿真器,建立了调厚过程压下系统和变形区的动态模型.仿真时,仿真器实时并行地计算带钢和轧机的模型, 计算机控制系统的控制器运行AGC软件,两者通过内存映像网实时交换数据,因此通过虚拟的对象实现了对AGC软件的实时离线调试

在LECO436氧氮分析仪上研究了1600~2813℃温度范围内钢液脱氮动力学。结果表明:温度低时,脱氮受液相边界层传质及界面化学反应混合控制,温度高时,脱氮受液相边界层传质过程控制。在2250℃以下,温度对k1'的影响服从Arrhenius公式。硫对脱氮的阻碍作用随着温度的升高而降低,在温度2250℃以上,硫的表面活性作用消失

1 8.1 Controller Parameterization for General Plants 2 8.2 H∞ PID Controllers for Unstable Plants 3 8.3 H2 PID Controllers for Unstable Plants 4 8.4 Performance Limitation and Robustness 5 8.5 Maclaurin PID Controllers for Unstable Plants 6 8.6 PID Design for the Best Achievable Performance 7 8.6 All Stabilizing PID Controllers for Unstable Plants