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VAPOR PRESSURE AT TOP OF LPG STORAGE SPHERE

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tommy11

Mechanical
Joined
Mar 8, 2009
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17
Location
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
 
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.

Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
 
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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