Parallel Switching Regulatory Control of Iron Ore Flowrate from Multiple Feeders with Time Delay

Sidney Viana
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Abstract

The suitable performance of an industrial process needs regulatory control loops to adjust the main process variables to their especified reference values (set-points), and to compensate eventual load disturbances on the process. Regulatory control is fundamentally used in the industry for stabilizing process variables, and it’s generally implemented through the SCADA architeture of the plantwide control system. The absence or inefficiency of control in an industrial process generally implies in losses of productivity so that regulatory control is a key issue for improving process performance. In this context, this article presents the development and implementation of a control strategy for regulating the output mass flow (in t/h) of a crushing plant in the Carajás Iron Ore Processing Factory. The plant has eight feeders in parallel, and the goal was to control such feeders so that the resulting output flow matches a specified production set-point (in t/h). The article first explains the process, the control problem, and the transfer function model of the process. Subsequently, one’s presented the control strategy, which was based on a switching between a constant and a PI control action. The suitability of the strategy was investigated through computational simulations. Finally, the results and conclusions are discussed
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具有时滞的多给矿机流量并联切换调节控制
工业过程的适当性能需要调节控制回路将主要过程变量调整到其指定的参考值(设定点),并补偿过程中的最终负载干扰。在工业中,调节控制基本上用于稳定过程变量,它通常通过工厂控制系统的SCADA架构实现。工业过程中缺乏控制或控制效率低下通常意味着生产力的损失,因此管制控制是改善过程性能的关键问题。在此背景下,本文介绍了Carajás铁矿石加工厂破碎厂输出质量流量(t/h)调节控制策略的开发和实施。该工厂有8个平行的给料机,目标是控制这些给料机,使输出流量符合指定的生产设定值(单位为t/h)。本文首先阐述了过程、控制问题以及过程的传递函数模型。随后,有人提出了控制策略,该策略基于常数和PI控制动作之间的切换。通过计算机仿真研究了该策略的适用性。最后,对研究结果和结论进行了讨论
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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