Design and comparison of two PID control strategies to improve the performance of the boiler unit in a steam power plant

S. Khodakaramzadeh, H. Moradi
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Abstract

In this paper, two PID-based control strategies are proposed to improve the performance of an industrial boiler unit in the steam power plant. A multivariable dynamic model of the boiler unit of a certain steam power plant is considered. Output variables of the dynamic system including the water level of drum, drum pressure and steam temperature are controlled via the manipulation of input variables including the feed water, fuel and spray attemprator mass rates. To design the controllers, two cases are considered for the dynamics of the boiler unit. First, it is considered as a multi SISO (single input-single output) models while in the second case, it is considered as a MIMO (multi inputs-multi outputs) model. For these cases, two PID controllers in the configuration of a diagonal and a lower triangular matrix gain are designed. The objective of the control strategy is to improve the dynamic system performance in the presence of perturbations in output variables. The effectiveness of the proposed PID controllers in tracking of desired objectives and required variation of control efforts is compared.
设计并比较了两种PID控制策略以提高某电厂锅炉机组的性能
本文提出了两种基于pid的控制策略,以提高蒸汽发电厂工业锅炉机组的性能。考虑了某蒸汽发电厂锅炉机组的多变量动态模型。动态系统的输出变量包括汽包水位、汽包压力和蒸汽温度,通过操纵输入变量包括给水、燃料和喷雾调节剂质量率来控制。在设计控制器时,考虑了锅炉机组的两种动态情况。首先,它被认为是一个多SISO(单输入-单输出)模型,而在第二种情况下,它被认为是一个MIMO(多输入-多输出)模型。针对这些情况,设计了对角线增益和低三角矩阵增益配置的两个PID控制器。该控制策略的目标是在输出变量存在扰动的情况下改善动态系统的性能。比较了所提PID控制器在跟踪期望目标和所需控制努力变化方面的有效性。
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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