QRA FAR FN-Curve ISO-Risk Individual Risk computations, Risk levels quantitative risk analysis software Air Dispersion modeling software Fire explosion

HAMS-GPS Quantitative Risk Assessment Software

FAR, FN-Curve, ISO-Risk, Individual Risk computations, Risk levels

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HAZOP Software (Advanced)	QRA modeling software (Accidental release of hazardous chemicals)	Air dispersion modeling software (Air, gas, Stack gas dispersion modeling software)
Fire load calculation software
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Snapshots of advanced QRA software
Accidental release of hazardous chemicals
Plume, Puff, Spill Dispersions based on Gaussian dispersion calculations and modeling, with tabular and graphic display with 6-User defined Isopleths in XY-Slice at Y-Cross wind distance. Full 3-D “CAT-Scan” output possible with dispersion “Cake slicing in XY (Isopleth) Graphs. Graphics are in colour. It is a complete CAT-Scan with Probits (PROBIT short for Probability Unit, is the percent Fatality and Injury due to exposure to any hazardous agent.). This Advanced Dispersion provides for Mass and volumes of various concentration zones and concentration zone shells of Plumes, Puffs and Spill pool evaporation dispersions. Free spread Pool fire, Dyke Pool fire, Tank fire, jet fire, fireball, flash fire, with PROBITs. Graphics are in colour UVCE, BLEVE, Under ground explosions, mechanical explosions-cylindrical vessel, spherical vessel, Dust explosion with PROBITs. Graphics are in colour. FAR, FN-Curve, ISO-Risk, Individual Risk computations,Risk levels from 10^-2 to 10^-10. Quantitative risk analysis is required to provide a numerical and objective understanding of project risks, facilitating more informed decision-making and resource allocation. It helps to identify, assess, and manage risks by quantifying their potential impact on various project aspects like cost, time, and scope. Objective Decision-Making: Quantitative analysis reduces subjectivity by providing numerical data, making it easier to assess the magnitude of risks and make informed decisions about project management. Scenario Analysis: It allows for simulating different scenarios and understanding the potential impact of various risk events on the project, enabling better preparedness and strategic planning. Resource Allocation: By quantifying potential costs and time delays, projects can allocate resources more effectively to mitigate high-impact risks and ensure project success. Improved Risk Management: It helps identify the most significant risks and allows for focused mitigation strategies, preventing waste of resources on insignificant risks. Contingency Planning: Quantitative analysis provides a basis for creating contingency plans and reserves, ensuring that projects can be managed effectively in the face of unforeseen events. Regulatory Compliance: Many regulations require organizations to conduct quantitative risk assessments to evaluate and manage risks associated with specific activities, such as those in the finance, healthcare, or energy sectors. Enhanced Project Success: By understanding the potential impact of risks, projects can be managed more effectively, increasing the likelihood of achieving project goals and objectives.	Help on how to do BLEVE simulations BLEVE (Boiling Liquid Expanding Vapour Explosion) scenarios A BLEVE is an explosion caused by a liquid, which is boiling and continuing to produce vapour.If the chemical is flammable, it is likely that the resulting cloud of the substance will ignite after the BLEVE has occurred, forming a fireball and possibly a fuel-air explosion. BLEVEs, which result in very large fireballs, occur when process vessels containing flammable materials with high vapour pressures are exposed to significant external heat. If Liquid is flammable flashing liquid or flammable liquid: BLEVE scenarios Under explosion scenario options Tank-over heating by external source or Mechanical Explosion leading to BLEVE scenario (CnE) Tank-over heating by external source or Mechanical Explosion puff delayed internal ignition leading to Unconfined vapour cloud explosion BLEVE scenario (UCE)" Under fire scenario options Tank over heating by external source puff Immediate Edge Ignition leading to Fire Ball leading to BLEVE scenario If Liquid is non-flammable Mechanical Explosion scenario Under explosion scenario options Tank-over heating by external source leading to Mechanical Explosion (CnE) Graphics mapping are in colour Graphs can be plotted to scale on Site Maps both in Graphics and AutoCAD .dwg files.

Watch QRA software package Demo on YouTube	Download or view demo videos HD quality use Google chrome browser.
Dispersion (1 of 4) https://youtu.be/Ov56DCsqXkI Explosion (2 of 4) https://youtu.be/bj-hrYyh1Mo Fire (3 of 4) https://youtu.be/13O1J7PFnBY Risk Assessment (4 of 4) https://youtu.be/NVswC5uKp10 Calculate rate of accidental release of hazardous chemical Recalculating rate of release https://youtu.be/YAcgID9Z2j0	1 Dispersion modeling 2. Explosion modeling 3. Fire modeling 4. Risk Assessment modeling 5. Calculate rate of accidental release of hazardous chemical 6. Recalculating rate of release