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Dynamic modelling and control strategies for flexible operation of amine-based post-combustion CO2 capture systems

机译:基于胺基燃烧二氧化碳捕获系统灵活运行的动态建模与控制策略

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The abatement of anthropogenic CO2 gas and extensive demand for electrical energy has motivated cleaner power production from fossil fuels. This paper presents a mechanistic model of amine-based post-combustion CO2 capture (FCC) process. Validation of the proposed model is performed using pilot plant data available from literature. Process control analysis is then performed using this model whereby three control schemes are proposed; a standard PID feedback control scheme, a cascade-PID scheme and thirdly a model-based strategy in the form of model predictive control (MPC). Stepwise set point tracking and disturbance rejection scenarios are employed to evaluate the performance of the proposed controllers for flexible operation, i.e., under variable plant load condition surrogate to electricity and carbon market prices patterns. Three elements of constraints include operational, economic and environmental are considered in selecting the best control strategy. The closed-loop simulation results showed that the MPC strategy handles very well the servo and regulator problems without violating the above mentioned constraints. (C) 2015 Elsevier Ltd. All rights reserved.
机译:削弱人为CO2气体和对电能的广泛需求具有来自化石燃料的促进净功率。本文介绍了基于胺的燃烧后CO2捕获(FCC)过程的机械模型。使用从文献中提供的试验工厂数据进行拟议模型的验证。然后使用该模型进行过程控制分析,其中提出了三种控制方案;标准PID反馈控制方案,Cascade-PID方案,第三个是模型预测控制(MPC)形式的基于模型的策略。采用逐步设定点跟踪和扰动抑制方案来评估所提出的控制器的性能,以实现灵活的操作,即,在可变植物负载条件下的电力和碳市场价格模式。三个限制要素包括在选择最佳控制策略方面考虑运营,经济和环境。闭环仿真结果表明,MPC策略在不违反上述约束的情况下处理伺服和调节器问题非常好。 (c)2015 Elsevier Ltd.保留所有权利。

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