Approach for hazard identification
Assessments such as Hazard and Operability (HAZOP), Hazard Identification (HAZID), Process Hazard Analysis (PHA), and Layer of Protection Analysis (LOPA) are essential for ensuring the safety and reliability of operation in the process industries. These exercises involve technical professionals who identify the most significant hazards present within a unit, based on hazardous (flammable and toxic) materials, their volume, storage conditions, and potential cause of loss of containment. This is a key step as identifying hazards present on a site and in its operations help prevent or reduce the potential accidental releases of hazardous materials.
Estimating the possible consequences during a process hazard analysis is usually done in a qualitative manner.
No. | Primary Guideword | Secondary Guideword | Potential Hazard | Failure Mode / Cause | Unmitigated Consequences | Safeguards |
---|---|---|---|---|---|---|
No.1
|
Primary GuidewordLoss of containment |
Secondary GuidewordJoint / Fitting
|
Potential HazardY
|
Failure Mode / CauseJoint Failure
|
Unmitigated Consequences
|
Safeguards
|
When more accurate evaluation of the potential consequences of low-consequence hazards, or when a more thorough assessment of these hazards is required, quantitative analysis of release scenarios can be performed.
The tool suitable for estimation of consequences
Phast™ is DNV’s consequence analysis software suitable for the process industries. It uses validated mathematical models to simulate the behaviour of hazardous substances upon release, considering factors such as type of release, the properties of the substances, and weather conditions. The tool provides comprehensive results and visual representation in the form of graphs for discharge, dispersion, thermal, overpressure, and toxic effects.
A typical workflow within Phast involves the following steps:
By following the steps above, technical professionals can estimate the potential consequences of hazardous releases.
The inputs necessary for performing consequence modelling in Phast are typically obtained from:
- Process and instrumentation diagrams (P&IDs)
- Process flow diagrams (PFDs)
- Plot plans
- Heat & mass balances
- Equipment ratings and data sheets
- Operating procedures
No. | Primary Guideword | Secondary Guideword | Potential Hazard | Failure Mode / Cause | Unmitigated Consequences | Safeguards |
---|---|---|---|---|---|---|
No.1
|
Primary GuidewordLoss of containment |
Secondary GuidewordJoint / Fitting
|
Potential HazardY
|
Failure Mode / CauseJoint Failure
|
Unmitigated Consequences
Quantified Results:
|
Safeguards
|
In addition to numerical calculation results, Phast provides visual representation of the consequences, which are commonly reviewed during a process hazard analysis. The visualisation of results is crucial during workshops and Phast facilitates this by allowing for consequences results from release scenarios to be overlaid on satellite imagery or plot plans. This feature provides technical professionals with confidence when evaluating hazardous scenarios.
For example, the figure illustrates the thermal radiation hazard ranges for multiple radiation levels. This demonstrates the value of Phast to provide a clear understanding of potential hazards during hazard workshops.
Explore our software solution:
Phast
Control your hazards by modelling discharge, dispersion, fires, explosions and toxic effects.
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