I'm a process engineer attempting to calculate the pressure increase of a few liquid chemicals due to thermal expansion within a pipe. The purpose is to determine if the selected pipe will withstand the expansion and whether or not a PSV is necessary. I'm using methanol and ethanol as similar substitutes for the chemicals of concern. I'm worried that my calculations are incorrect because with a temperature increase from 75F to 100F, I'm resulting in an increase of over 1000psi. The equation I'm using is from API 521.
I've had a very difficult time determining the isothermal compressibility coefficient, so I feel as though that is where the equation is going wrong. The values I have are both roughly 8.0E-06 1/psi for this coefficient. Does this seem correct? Is there another section of the equation that may be causing such a large increase? Any advice on this calculation is appreciated.
Thank You.