I'm trying to size a safety relief valve for a 2-phase separator.
Per the Crosby Pressure Relief Valve Engineering Handbook:
W = Q/Hvap
Where:
W = Mass flow, lbs/hr
Q = Total heat absorption to the wetted surface, BTU/hr
Hvap = Latent heat of vaporization, BTU/lb
My problem is Hvap. It's easy to look up Hvap for a given pure fluid at atmospheric pressure, but how does one go about calculating/estimating Hvap for an oil-water-gas mixture at 250 psi.
Is this something that has to be measured using a sample of the emulsion? Or is there a "trick" or "industry standard" that I can use to get around this hangup.
Thanks,
Luke
Per the Crosby Pressure Relief Valve Engineering Handbook:
W = Q/Hvap
Where:
W = Mass flow, lbs/hr
Q = Total heat absorption to the wetted surface, BTU/hr
Hvap = Latent heat of vaporization, BTU/lb
My problem is Hvap. It's easy to look up Hvap for a given pure fluid at atmospheric pressure, but how does one go about calculating/estimating Hvap for an oil-water-gas mixture at 250 psi.
Is this something that has to be measured using a sample of the emulsion? Or is there a "trick" or "industry standard" that I can use to get around this hangup.
Thanks,
Luke