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VAPOR PRESSURE AT TOP OF LPG STORAGE SPHERE

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tommy11

Mechanical
Mar 8, 2009
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DZ
Hi,
what would be the LPG vapor minimum design pressure at the top of the sphere as per good engineering practice and which parameters are considered to fix it?

Thank's
 
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Actual composition of "LPG" varies so you need to know this plus the maximum liquid temperature.

Then you can find the vapour pressure.

Rather basic question.

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Vessels holding non refrigerated LPG are specified with an upper design pressure of approx. 20barg. Generally, commercial grade LPG has a sat vapor pressure of about 14barg at 38degC. You can make a good first approximation by looking up sat vap pressure curve for pure propane, and find the sat vap pressure at the max normal operating day time temperature at your location.
 
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