Sakthi Prasanth Aenugula , Aswin Chandrasekar , Prashant Mhaskar , Thomas A. Adams II
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引用次数: 0
摘要
半连续蒸馏是一种分离技术,用于提纯中低产量的多组分混合物。这项研究解决的问题是设计一种数据驱动的模型预测控制 (MPC) 方法,使半连续工艺每处理一吨原料的年化总成本 (TAC) 最小化,同时保持所需的产品纯度。手稿使用从 Aspen Plus Dynamics 仿真中收集的数据作为测试平台,展示了数据驱动技术的实施,以取代通常不可用的第一原理模型。采用子空间模型识别技术来开发多模型框架,以捕捉工艺的动态行为,然后在收缩地平线 MPC (SHMPC) 方案中加以利用,以实现所需的目标。模拟结果表明,与之前研究中使用的传统 PI 设置相比,每吨进料的 TAC 降低了 11.4%。
Minimizing total annualized cost per tonne of feed processed of a semicontinuous distillation process utilizing data-driven model predictive control
Semicontinuous distillation is a separation technique used to purify multicomponent mixtures with low to medium throughput. This research addresses the problem of designing a Data-driven Model Predictive Control (MPC) approach that enables minimizing the Total Annualized Cost (TAC) of the semicontinuous process per tonne of feed processed while maintaining the required product purity. In lieu of typically unavailable first principles models, the manuscript demonstrates the implementation of data-driven technique using data collected from an Aspen Plus Dynamics simulation as a test bed. A subspace model identification technique is adapted to develop a multi-model framework to capture the dynamic behavior of the process and then utilized within a Shrinking Horizon MPC (SHMPC) scheme, to achieve the required objective. The simulation results demonstrate a lowering of the TAC/tonne of feed by 11.4% compared to the traditional PI setup used in the previous studies.
期刊介绍:
Computers & Chemical Engineering is primarily a journal of record for new developments in the application of computing and systems technology to chemical engineering problems.