在实时优化器架构中部署一种新型软传感器以提高硫回收装置的完整性和能效

Satyadileep Dara, I. Khan, Eisa Salem Al Jenaibi, Subhendu Sengupta, Vincent Goveas, Nawal Al Yahyaee, S. Ibrahim, A. Jagannath, A. Raj
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引用次数: 0

摘要

目前还没有用于测量克劳斯炉出口气体中芳烃的商用分析仪,这导致了能源效率的次优,并带来了资产完整性问题。为了解决这个问题,开发了一个高保真模型作为实时分析仪。本研究的目的是将软传感器整合到实时优化器(RTO)的架构中,以监测克劳斯炉出口流中芳烃的存在。软传感器集成在RTO服务器中,该服务器提供对工厂运行数据和DCS(分布式控制系统)的访问。RTO中的软传感器功能包括以下步骤:软传感器访问工厂数据并收集仿真所需的输入数据RTO中可用的仿真软件执行软传感器模型仿真并生成芳烃成分数据芳烃成分数据作为软测量写入DCS接口,操作员监控芳烃成分并相应地调整燃气燃烧芳烃软传感器作为动力学模型开发;它是克劳斯炉几个关键反应速率参数的函数。将克劳斯炉的动力学模型纳入到过程仿真模型中,并对催化转化器进行了仿真。用大型工厂数据对模型进行了验证,结果表明模型预测炉温误差在+/- 5%以内,芳烃成分误差在+/- 5ppm以内。仿真分析表明,在保证不发生BTEX滑移的情况下,炉温可降低至少5℃。这种炉温的变化导致燃料气体流量减少约200 Nm3/h,相当于每年50万美元的经济效益。软传感器的部署目前正在通过与RTO许可方的合作进行。据笔者所知,目前市场上还没有能够充分模拟芳烃氧化现象和预测炉出口芳烃含量的模拟器。这种软传感器是新型的,也是同类产品中的第一个,有望实现可持续的能源效率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Deployment of a Novel Soft Sensor in the Real Time Optimizer Architecture to Enhance the Integrity and Energy Efficiency of Sulfur Recovery Units
Commercial analyzers for measuring the aromatics in the Claus furnace exit gas are currently not available and this leads to sub-optimal energy efficiency and poses asset integrity concerns. To address this problem a high-fidelity model is developed to function as a real time analyzer. Objective of this work is to incorporate the soft sensor in the architecture of Real Time Optimizer (RTO) to monitor the presence of aromatics in the Claus furnace exit stream. The soft sensor is incorporated in the RTO server which provides the access to the plant operating data and the DCS (Distributed Control System). Soft sensor function in the RTO involves the following steps: Soft sensor accesses the plant data and collects the needful input data for simulation Simulation software available in the RTO executes the softs sensor model simulation and generates the aromatics composition data Aromatics composition data is written to the DCS interface as a soft measurement Operators monitor the aromatic composition and accordingly adjust the fuel gas firing Aromatic soft sensor is developed as a kinetic model, which is function of rate parameters of several key reactions of the Claus furnace. The kinetic model of the Claus furnace is incorporated in a process simulation model and catalytic convertors are simulated too. Model is validated with large plant data to show that model predicts furnace temperature within +/- 5% error and aromatics composition within +/- 5 ppm. Simulation analysis shows that the furnace temperature can be decreased by at least 5 °C while ensuring no BTEX slip. Such change in furnace temperature leads to a reduction in fuel gas flow by ~200 Nm3/h, which translates to a monetary benefit of 0.5 million $/yr. Deployment of the soft sensor is currently in progress through engagement with RTO licensor. To the best knowledge of authors, currently, there is no simulator in the market which can adequately model aromatics oxidation phenomena and predict the aromatic content in the furnace exit. This soft sensor being deployed is novel and first of its kind and expected to achieve a sustainable energy efficiency.
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