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石油化工装置动态风险监测模型的构建与应用研究OA

Research on the Construction and Application of Dynamic Risk Monitoring Model for Petrochemical Units

中文摘要英文摘要

为解决石油化工装置动态风险监测滞后、动静风险割裂及重大信号易被低估的问题,构建了一种基于多源数据融合的动态风险监测模型.模型以事故致因理论为基础,通过梳理屏障类型确定指标权重,结合动态与静态指标实现风险状态的综合表征.动态指标涵盖工艺参数报警、安全仪表系统(Safe-ty Instrumented System,SIS)投用状态、设备状态监测等数据,以5 min 为间隔进行计算;其中,气体检测系统(Gas Detection System,GDS)报警与火灾报警被设为"一票晋级项"(指一旦触发,模型直接判定为最高风险等级).静态指标以24 h 为周期更新,通过修正系数对动态风险值进行调整.模型在某脱硫装置中进行了417 d 的实证验证,处理动态数据 12 万余组、静态数据 417 组.验证期内,与人工巡检模式相比,隐患发现量提升37%,非计划停车次数由3 次降至1 次.上述结果为该模型在石油化工装置风险预警中的应用提供了数据支撑.

To address the issues of delayed dynamic risk monitoring,the disconnection between dynamic and static risks,and the frequent underestimation of critical signals in petrochemical units,this study developed a dynamic risk monitoring model based on multi-source data fusion.Grounded in accident causation theory,the model determined indicator weights by categorizing safety barrier types,thereby achieving a comprehensive char-acterization of risk status through the integration of dynamic and static indicators.Specifically,dynamic indica-tor-encompassing process parameter alarms,the operational status of the Safety Instrumented System(SIS),and equipment condition monitoring data-were calculated at 5-minute intervals.Notably,Gas Detection System(GDS)and fire alarms were designated as"one-vote escalation"criteria,meaning that their activation instantly elevates the model′s output to the highest risk level.Concurrently,static indicators were updated on a 24-hour cycle to adjust the dynamic risk values using correction coefficients.The proposed model was validated in a des-ulfurization unit over a 417-day period,processing more than 120 000 sets of dynamic data and 417 sets of static data.The results indicated that,compared to traditional manual inspection methods,the detection of hidden hazards increased by 37%,while the frequency of unplanned shutdowns decreased from three to one during the validation period.Consequently,these findings provide support for the application of the proposed model in risk early warning systems for petrochemical facilities.

杨冬;王辉;薛永鸿;苏沫林;阎红巧

中国石油天然气股份有限公司兰州石化分公司,甘肃 兰州 730030中国石油天然气股份有限公司兰州石化分公司,甘肃 兰州 730030中国石油天然气股份有限公司兰州石化分公司,甘肃 兰州 730030中国石油集团安全环保技术研究院有限公司,北京 102206中国石油集团安全环保技术研究院有限公司,北京 102206

化学化工

Bowtie理论风险管控状态监测动态模型安全仪表系统气体检测系统

Bowtie theoryrisk controlcondition monitoringdynamic modelSafety Instrumented System(SIS)Gas Detection System(GDS)

《安全、健康和环境》 2026 (4)

8-15,8

10.3969/j.issn.1672-7932.2026.04.002

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