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contributor authorJian-Ping Zhao
date accessioned2017-05-09T00:35:12Z
date available2017-05-09T00:35:12Z
date copyrightApril, 2009
date issued2009
identifier issn0094-9930
identifier otherJPVTAS-28506#024503_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/141860
description abstractThe high-pressure hydrogenation cracking unit is the core equipment system in the aromatic hydrocarbon factory, which is subjected simultaneously to the action of hydrogen, high pressure, and high temperature. In this paper, quantitative analysis method of risk-based inspection (RBI ) was carried out with a commercially available RBI software. In API 581, the risk situation for each type of equipment in the system was classified into four grades: low-risk grade, medium-risk grade, medium-high-risk grade, and high grade. This is expressed as a risk matrix. The entire risk distribution of 553 equipment and/or piping items of the systems that compose the unit was obtained. The hydrocracking reactors and the reactor effluent air coolers are in the “medium-high-risk” category. Based on the RBI results, an optimum inspection plan was developed by the author to reduce the risk level for the hydrogenation cracking unit. Upon validation of the inspection activity in 2004, it is concluded that the optimum inspection plan was in compliance with the engineering specification of the aromatic hydrocarbon factory.
publisherThe American Society of Mechanical Engineers (ASME)
titleRisk-Based Inspection Analysis for High-Pressure Hydrogenation Cracking Unit
typeJournal Paper
journal volume131
journal issue2
journal titleJournal of Pressure Vessel Technology
identifier doi10.1115/1.3006949
journal fristpage24503
identifier eissn1528-8978
keywordsInspection
keywordsHigh pressure (Physics)
keywordsFracture (Process)
keywordsPipes
keywordsFailure AND Corrosion
treeJournal of Pressure Vessel Technology:;2009:;volume( 131 ):;issue: 002
contenttypeFulltext


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