Dynamic modeling of heating furnace & enhancing the performance with PIλDμ controller for fractional order model using optimization techniques

Amlan Basu, Sumit Mohanty, Rohit Sharma
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引用次数: 4

Abstract

Over the year heating furnace system has always suffered a huge loss of heat energy the line of safety of man power. The flow of fuel into chamber of furnace, basically limits the gas pressure inside furnace. So, proper relation between fuel flow rate and gas pressure inside furnace is essential to ensure a proper utilization of heat with minimum settling time and minimum overshoot, so that safety is not compromised. This paper enlightens design of a proper integer order model (IOM) of heating furnace which is further converted into a fractional order model (FOM). This fractional order model is used with PID controllers in closed loop. For enhancing the performance of PID controller, fractional elements are used. Therefore, PIλDμ controller is optimized properly for a smooth, low overshoot response with a very low settling time. These proposed results may be implemented properly in small scale furnaces or large scale industrial furnaces.
加热炉的动态建模&用优化技术提高分数阶模型的pi - λ dμ控制器性能
多年来加热炉系统一直遭受着巨大的热能损失,线路安全用人力大。燃料流入炉膛,基本上限制了炉膛内的气体压力。因此,合理调整炉内燃料流量与燃气压力的关系,以保证热量的合理利用,保证最小的沉淀时间和最小的超调量,不影响安全。本文对加热炉合理的整数阶模型的设计提出了启发,该模型可进一步转化为分数阶模型。该分数阶模型用于PID控制器的闭环控制。为了提高PID控制器的性能,采用了分数阶元件。因此,pi - λ dμ控制器经过适当优化,具有平滑、低超调响应和极低的沉降时间。这些建议的结果可以在小型炉或大型工业炉中适当地实施。
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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