Starting with a feasible incident (such as activation of a relief device, catastrophic failure of equipment or loss of containment) for a specific item of equipment, the potential causes and outcome may be determined. HAZOP “parameters” associated with control of the process such as temperature, pressure and flowrate; and “deviations” from the design intent such as high pressure, low temperature or no flow may be utilized in a simple Fault Tree to identify causes for hazardous situations that could lead either directly or indirectly to an incident. The feasibility of various outcomes (such as vapor cloud explosion or toxic infiltration to an occupied building) resulting from the incident may be evaluated using a simple Event Tree to complete the initial description of a hazard scenario.
See more of this Group/Topical: Global Congress on Process Safety
