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Dynamic safety analysis of process systems with an application to a cryogenic ammonia storage tank

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dc.contributor.author Aneziris, ON en
dc.contributor.author Papazoglou, IA en
dc.contributor.author Lygerou, V en
dc.date.accessioned 2014-03-01T01:15:33Z
dc.date.available 2014-03-01T01:15:33Z
dc.date.issued 2000 en
dc.identifier.issn 0950-4230 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/13589
dc.subject dynamic reliability en
dc.subject ammonia storage en
dc.subject Markovian analysis en
dc.subject risk assessment en
dc.subject dynamic safety en
dc.subject quantified risk assessment en
dc.subject.classification Engineering, Chemical en
dc.subject.other RELIABILITY-ANALYSIS en
dc.subject.other DYLAM APPROACH en
dc.title Dynamic safety analysis of process systems with an application to a cryogenic ammonia storage tank en
heal.type journalArticle en
heal.identifier.primary 10.1016/S0950-4230(99)00060-1 en
heal.identifier.secondary http://dx.doi.org/10.1016/S0950-4230(99)00060-1 en
heal.language English en
heal.publicationDate 2000 en
heal.abstract A method for calculating the dynamic reliability of safety systems and its application to a refrigerated liquid cryogenic ammonia storage tank is presented. The method is based on the theory of Markov chains and can model dynamic phenomena of the process and its safety systems. It offers the capability of modelling realistically the competing process of repairing failed safety systems and the exceeding of safe limits by some critical physical parameters of the process. The results of the Markovian analysis are compared to those of the classical Fault Tree/Event Tree methods and it is shown that the proposed method offers a substantial improvement over the classical approach. The probability of failure from overpressure of a cryogenic ammonia storage tank depends in general on the level of the ammonia in the tank at the time of accident initiation. Assuming a uniform distribution for the ammonia level in the tank, the average upper and lower limits for the failure probability over a year provided by the FT/ET methods span three orders of magnitude [1.4x10(-1)-1.0x10(-4)] depending on whether repair is considered or not. The proposed approach realistically determines this failure probability at 3.3x10(-3). Additional results from specific levels of ammonia are also provided. (C) 2000 Elsevier Science Ltd. All rights reserved. en
heal.publisher ELSEVIER SCI LTD en
heal.journalName JOURNAL OF LOSS PREVENTION IN THE PROCESS INDUSTRIES en
dc.identifier.doi 10.1016/S0950-4230(99)00060-1 en
dc.identifier.isi ISI:000085386200006 en
dc.identifier.volume 13 en
dc.identifier.issue 2 en
dc.identifier.spage 153 en
dc.identifier.epage 165 en


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