聚酯生产过程的监控

S. Valluri, G. Lei, C. Porter
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引用次数: 0

摘要

提出了一种连续聚酯装置的实时监控策略。该过程包括三个反应步骤,即酯化反应、预聚反应和终聚反应。本文主要研究预聚合反应器。建立了一种高效、准确的高保真动态模型,用于实时监测和控制。由于本研究的重点是实时监测和控制应用,因此模型的开发、配置和实现使用实时动态仿真软件SimSuite Pro/sup TM/进行,该软件与工厂分布式控制系统D/3 DCS/sup TM/串联运行。利用该模型,建立了聚酯分子量和羧酸浓度的多速率控制策略。除了快速测量,即温度和压力,该控制器还采用慢速测量,即分子量和酸浓度。在没有慢速测量的情况下,使用动态模型的估计。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Monitoring and control of polyester production process
A real-time monitoring and control strategy is presented for a continuous polyester plant. This process consists of three reaction steps, namely, esterification, prepolymerization, and finishing polymerization. This paper is focused on the prepolymerization reactor. A high-fidelity dynamic model that is efficient and accurate for real-time monitoring and control is developed. As this study is focused on real-time monitoring and control applications, the model development, configuration, and implementation are performed using a real-time dynamic simulation software, SimSuite Pro/sup TM/, running in tandem with the plant distributed control system, a D/3 DCS/sup TM/. By using this model, a multirate control strategy is developed for polyester molecular weight and carboxyl acid concentration control. In addition to the fast measurements, i.e. temperature and pressure, this controller also utilizes slow measurements, i.e. molecular weight and acid concentration. In the absence of slow measurements, the estimates from the dynamic model are used.
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