VTB001
Petroleum
- Oct 11, 2006
- 2
Hello; I have a theoretical waste stream (125F / 52 oC) that contains water with an extremely small amount of pentane in it. The stream has the potential to become open to atmosphere. I am trying to determine if I can calcualte the flash point (since I cannot open/close cup measure it) based on the amount of pentane vs water at this temperature and pressure.
I am concerned with the potential for this miniscule amount of pentane to be a flammable concern if opened to atmosphere(assuming the low C5 / H2O ratio is maintained). Although insoluable in water, I do not think using the flash point of pentane is correct for this mixture but am not sure.
The flash point for pentane is -56F / -49 oC.
The boiling point is 97F /36 oC .
Vapour density is 2.5 (vs 1 for air)
I believe that there will be vapours produced wtih these temperatures (operating @ 125F with hydrocarbon flash point of -56F) which can be released when open to atmosphere.
I have not been able to find any reference to this in NFPA references but I may have missed it. Any advise would be appreciated. Thank you.
I am concerned with the potential for this miniscule amount of pentane to be a flammable concern if opened to atmosphere(assuming the low C5 / H2O ratio is maintained). Although insoluable in water, I do not think using the flash point of pentane is correct for this mixture but am not sure.
The flash point for pentane is -56F / -49 oC.
The boiling point is 97F /36 oC .
Vapour density is 2.5 (vs 1 for air)
I believe that there will be vapours produced wtih these temperatures (operating @ 125F with hydrocarbon flash point of -56F) which can be released when open to atmosphere.
I have not been able to find any reference to this in NFPA references but I may have missed it. Any advise would be appreciated. Thank you.