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Operational safety of an ammonia process network via model predictive control

机译:通过模型预测控制的氨过程网络的运行安全性

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Process safety is a crucial issue in the area of process systems engineering as accident prevention is a top priority in process operations. Operational safety needs to be directly incorporated into control system design to handle disturbances in the process. Motivated by the above considerations, this paper presents a practical application simulating multiple model predictive controllers within a multi-unit ammonia process, all of which integrate safety constraints of the process within their design. Specifically, catalytic deactivation in the shift reactor is a common and problematic disturbance that may trigger reaction thermal runaway in the methanator. Itwo controllers designed with the objective of improving operational safety are implemented on the ammonia plant under catalyst deactivation. Aspen Plus is a commercial process simulation software which is integrated with Matlab to run a closed-loop simulation for the ammonia process. The results demonstrate that under suitable design of the controllers, desirable closed-loop performance is achieved with high temperature extremities avoided during operation. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:过程安全是过程系统工程领域的一个关键问题,因为事故预防是过程操作中的首要任务。需要直接纳入控制系统设计中的操作安全,以处理过程中的干扰。通过上述考虑因素,本文提出了一种在多单元氨过程中模拟多模型预测控制器的实际应用,所有这些应用程序都将该过程的安全约束集成在其设计中。具体地,换档反应器中的催化失活是一种常见的且有问题的干扰,其可能引发甲烷罐中的反应热失控。目的是在催化剂失活下的氨植物上实施了具有改善操作安全性的目的的ITWO控制器。 Aspen Plus是一种商业流程仿真软件,它与MATLAB集成,以运行氨过程的闭环仿真。结果表明,在控制器的合适设计下,在操作期间避免的高温末端实现了所需的闭环性能。 (c)2019化学工程师机构。 elsevier b.v出版。保留所有权利。

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