I need an equation for calculating the volume of a partially filled ASME F&D head on a vertical tank. If anyone can help me out I would appreciate it. Thanks in advance.
I went through my reference books and even managed to dig out (after finding it) some old engineering documents I hoped might have it with no success. Horizontal, yes. Vertical, no.
However, the GPSA data book has a tabular set of data for the fractional volume of a vertical head at different liquid depths. You might want to try curve fitting a set of data points depending on the accuracy you need.
Thanks for the replies. For anyone who may need similar information, I got the following formulas from Chicago Bridge & Iron Co bulletin #594, page 7:
Volume or contents of partially filled hemi-ellipsoidal heads with major axis vertical
Q= Partially filled volume or contents in ft^3
V= Total volume of one head in ft^3
R= Radius of cylinder in ft
delta= a/(KR) where
a= liquid height
KR= head height
Upper head Q=1.5*V*(delta)*(1-(1/3*(delta)^2))
Lower head Q=1.5*V*(delta)^2*(1-(1/3*(delta))
It probably gives you the same result as the one refrenced above by mgp.
Unfortunately I was unable to find a formula for an ASME F&D head but I was able to fit a equation to curvature of tank in question. Using this, I can find the volume of a solid of revolution bound between the curve and a horizontal line at the liquid level. Kind of long but I think it will work close enough.
Gone are the days of everyone having the time to use second year university calculus and deriving the formulas from scratch by adding a couple of relatively simple integrals and solving for equation... I must be just too sentimental ...
Hey Delta, I don't know if those days are gone, or not. Last year I had to calculate the volume of a weir mounted up on the wall inside a vertical vessel. The weir was open at the top and trapeziodally-shaped in section. I had to calculate the volume (this was a skim trough in an IGF flotation cell) because the dump valve worked on a timer and we didn't want to blow a bunch of gas thru the dump valve and into the system. So I set up a double integral, roated it thru 2pi, and it worked. My old calc prof would have been proud. I even did it in the field, in the control room, in the rain, during a startup! How 'bout that! ;-) Thanks!
Pete
P. J. (Pete) Chandler, PE
Principal Engineer
Mechanical, Piping, Thermal, Hydraulics
Processes Unlimited International, Inc.
Bakersfield, California USA
pjchandl@prou.com