2011
DOI: 10.1016/j.psep.2011.03.002
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Conducting HAZOPs in continuous chemical processes: Part II. A new model for estimating HAZOP time and a standardized approach for examining nodes

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Cited by 8 publications
(4 citation statements)
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“…At each of these nodes, deviations in the process parameters are examined using the guide words (Dunj o et al, 2011a(Dunj o et al, , 2011b). To perform this task, the main causes that produce the performance deviations (i.e., failures or human errors), identified in step 2, can be easily used and added to the HAZOP worksheets (Fig.…”
Section: Description Of the Proposed Safety Methodologymentioning
confidence: 99%
“…At each of these nodes, deviations in the process parameters are examined using the guide words (Dunj o et al, 2011a(Dunj o et al, , 2011b). To perform this task, the main causes that produce the performance deviations (i.e., failures or human errors), identified in step 2, can be easily used and added to the HAZOP worksheets (Fig.…”
Section: Description Of the Proposed Safety Methodologymentioning
confidence: 99%
“…Substance cycles and establishments are by and large combustible, hazardous and harmful. In this manner, the distinguishing proof of these risks is fundamental to guarantee the protected plan and activity of these handling plants [4]. The number of procedures created to forestall mishaps in process ventures has expanded since the modern upheaval.…”
Section: Introductionmentioning
confidence: 99%
“…The HAZOP methodology was developed in the 1970s, when the growing size of chemical plants made a preventive approach necessary. In subsequent years, this methodology was applied to pharmaceutical [12], nuclear [13] and transportation [14] sectors and in continuous chemical processes [15,16].…”
Section: Introductionmentioning
confidence: 99%