akoester
Chemical
- Sep 14, 2012
- 7
I'm a Facilities Enigneer, and I recently started working in the Marcellus. A lot of the production units installed in Appalachia have meter runs integrated with the production unit skids (picture attached) - installed on the exterior of the cabinet. Our first generation pad design has the traditional set-up with separate meter houses, but the integrated design would save up significant space on the pads and time/materials for construction. I am working on reviewing the safety of this design. I believe the new hazard would be the potential for flash fire from the gas cloud released when changing the meter orifice plates.
I can quantify the volume of gas released from the chamber of the meter body when changing plates and I have the size of the orifice through which it is vented (1/4") - my question is how to then calculate the radius of flammability from the release to see if there is potential to reach the unit burner? My though was to calculate the release as dispersion from a single relief source. I have been reviewing API 521 section 6.3.2.2 Vapor emission. Would these equations be applicable if the release is indeed a (very short) jet exit?
Anyone else already using this design? Any suggestions on how to correctly evaluate the flash fire hazard?
I can quantify the volume of gas released from the chamber of the meter body when changing plates and I have the size of the orifice through which it is vented (1/4") - my question is how to then calculate the radius of flammability from the release to see if there is potential to reach the unit burner? My though was to calculate the release as dispersion from a single relief source. I have been reviewing API 521 section 6.3.2.2 Vapor emission. Would these equations be applicable if the release is indeed a (very short) jet exit?
Anyone else already using this design? Any suggestions on how to correctly evaluate the flash fire hazard?