- 1、本文档共22页,可阅读全部内容。
- 2、有哪些信誉好的足球投注网站(book118)网站文档一经付费(服务费),不意味着购买了该文档的版权,仅供个人/单位学习、研究之用,不得用于商业用途,未经授权,严禁复制、发行、汇编、翻译或者网络传播等,侵权必究。
- 3、本站所有内容均由合作方或网友上传,本站不对文档的完整性、权威性及其观点立场正确性做任何保证或承诺!文档内容仅供研究参考,付费前请自行鉴别。如您付费,意味着您自己接受本站规则且自行承担风险,本站不退款、不进行额外附加服务;查看《如何避免下载的几个坑》。如果您已付费下载过本站文档,您可以点击 这里二次下载。
- 4、如文档侵犯商业秘密、侵犯著作权、侵犯人身权等,请点击“版权申诉”(推荐),也可以打举报电话:400-050-0827(电话支持时间:9:00-18:30)。
查看更多
保护层分析-LayersOfProtAnalysis
? ABB - Page * Functional safety ? ABB - Page * E x t e n d e d A u t o m a t i o n S y s t e m 8 0 0 x A Functional safety Engineering - Layers of Protection Layers of Protection Analysis Fault Propagation Context Event Tree Method Layers of Protection Definition LOPA Event Tree Initiating Evnents and Failure Rates Example of Layers of Protection Fault Propagation modelling Analyze the Chain of events that leads to an accident Control System Fails Operator does not respond properly Mechanical relief failed Overpressure Event Initiating event Layers of Protection Analysis - LOPA A variant of Event Tree Analysis More structures Like event tree analysis, the initiating event start the chain of events Branches are layers of protection Consider only two outcome Accident No Event LOPA Version of Event Tree PL2, fails PL1, fails PL3, fails Accident Quantify using multiplications; all logical ANDs Ex, Column Rupture LOPA Draw the LOPA diagram for following situations Consequence of the accident = fire due to distillation column rupture has a root cause of loss of cooling water Layers of protection Operator respond to alarms and stops the process Process generally designed to withstand loss of cooling water The column has a pressure relief valve Source of ignition are controlled in the process area Ex: Column rupture LOPA LOPA Calculations Proceed as with event tree, but only need to calculate the frequency of accident Resulting accident frequency is initiating event frequency multiplied by PFD of all protection layers Example Cooling water failure frequency is 0,5/year Protection layers Operator response failure PFD = 0,15 Relief valve failure – PFD = 0,07 Process design inadequate – PFD = 0,01 Ignition source contacted – PFD = 0,3 Ex: Column Rupture, LOPA F=0,5/y * 0,15 * 0,01* 0,07 * 0,3 = 1,58E-5 per year Failure Rate Quantification Historical reliability data specific to your installation is best, but often difficult to get Plant maintenance and SIS fun
文档评论(0)