三区中温炉三通道PID控制器的合成

Alena I. Tsibina, G. P. Chikildin
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摘要

目前,在计量实验室中,需要通过再现国际温标的定点来从最高类别的标准转换温度单位。固定点的复制过程涉及金属的加热、熔化、过热和凝固,有时需要一个多工作日。这项工作的目的是创建并实际测试一种算法,该算法考虑了三区炉内的热流,以实现均匀加热和相对快速地到达凝固区域。在过去的二十年里,已经使用了几种算法,使得在一个工作日内完成所有四个阶段成为可能。本文介绍了一种经过实际测试的控制三区炉重现156.5985℃至1084.62℃温标定点的算法。它考虑了沿定点电池高度保持最小温度梯度的要求。该算法已在FSUE“VNIIFTRI”西西伯利亚分厂的高炉上得到应用。控制器模型基于自动控制理论的原理,采用多通道离散比例-积分-导数或PID控制器。根据系统结构对模型进行了修正。其主要思想是将三区炉模型表示为通道间相互影响的三通道控制对象。相应的控制器模型是一个三通道控制系统。在它的每个通道都有一个PID控制器。根据回放过程的阶段,三通道控制器改变其结构并调整其系数。这样的结构可以使炉达到足够的生产率。
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Synthesis of a three-channel PID controller for controlling a three-zone medium-temperature furnace
Currently, in metrological laboratories there is a need to transfer temperature units from standards of the highest category by reproducing the fixed points of the international temperature scale. The reproduction process of fixed point involves heating, melting, overheating and solidification of the metal and can sometimes take more than one working day. The purpose of this work was to create and practically test an algorithm that takes into account heat flows in a three-zone furnace for uniform heating and relatively fast reaching the solidification area. Over the past twenty years, several algorithms have been used making it possible to go through all four stages within one working day. This paper describes a practically tested algorithm for controlling three-zone furnaces for reproducing the fixed points of the temperature scale in the range from 156.5985 °C to 1084.62 °C. It takes into account the requirements for maintaining the minimum temperature gradient along the height of the fixed point cell. This algorithm has been used in the furnaces of the West Siberian branch of FSUE "VNIIFTRI". The controller model is based on the principles of automatic control theory using a multi-channel discrete proportional-integral-derivative or PID controller. The model was modified in accordance with the system structure. The main idea is to represent the model of a three-zone furnace as a three-channel control object with mutual influence between the channels. The corresponding controller model is a three-channel control system. In each channel of it there is a PID controller. Depending on the phase of the playback process, the three-channel controller changes its structure and tunes its coefficients. Such a structure made it possible to achieve sufficient productivity of the furnace.
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