dean427
Chemical
- Dec 5, 2010
- 24
Hello
I am currently assessing hydrocarbon pool fire formation from leak sources in an NGL/LPG service. My company has an internal quick reference flow chart to decide whether or not hydrocarbons released in the form of an aerosol jet could rain out and form a pool of liquids at grade. This flow chart is simple to use and all one needs is the normal boiling point of the liquid, the adiabatic flash fraction at 1 bar from MOP and the resulting adiabatic flash temperature. The problem is that I cant locate any engineers which understand the origin or the background of the limits on this decision tree. Therefore I feel that this is difficult to defend to health and safety regulators.
To demonstrate ALARP to a regulator we often make use of codes accepted by wider industry e.g. API codes. Does anyone know if there is an industry accepted method/code/best practice guideline to determining if hydrocarbons can rain out and form pools?
Many thanks
Dean
I am currently assessing hydrocarbon pool fire formation from leak sources in an NGL/LPG service. My company has an internal quick reference flow chart to decide whether or not hydrocarbons released in the form of an aerosol jet could rain out and form a pool of liquids at grade. This flow chart is simple to use and all one needs is the normal boiling point of the liquid, the adiabatic flash fraction at 1 bar from MOP and the resulting adiabatic flash temperature. The problem is that I cant locate any engineers which understand the origin or the background of the limits on this decision tree. Therefore I feel that this is difficult to defend to health and safety regulators.
To demonstrate ALARP to a regulator we often make use of codes accepted by wider industry e.g. API codes. Does anyone know if there is an industry accepted method/code/best practice guideline to determining if hydrocarbons can rain out and form pools?
Many thanks
Dean