Bobby,
Thanks for the answers. Let me explain what I guess:
Problem description: I want to recall that the problem only arises on summer, where the operator need more time to fill the trailer. Sometimes the operator open the vent valve to take out gas
Causes:
1) NPSH - I guess vapor on piping suction could be because of that. I do the maths and there´s no problem there.
2) Suction piping.
It is Far? YES de pump is 100 meters away from the bullet.
Slope? It seems that no slope (down or up) is present
Main or individual pipe? each pump has his own 6in pipe from bullet
Probably I could confirm that no line up exists to the pump (if any very small, no visible by eye)
3) Velocity?
Pump nominal flow is 45 m3/h - With 6in pipe we have 0.65 m/s. I think is a good velocity for suction piping.
4) Composition envelope?
Beside there´s more than one element, the behavior could be read as vapor -equilibrium data for the propane (hysys envelope attached)
at 40°C(104°F) 13.6 kg/cm2 (185 psi)
at 50°C (122 °F) 16.7 kg/cm2 (227psi)
al 52.5°C (125 °F) 17.5 kg/cm2 (241psi) PSV set on bullet.
If pipe is heated by solar radiation up to 52.5 °C and more, the psv would open to release pressure.
There´s any chance that a section of the pipe could vaporize? Need some help here-. Because I have doubt here, y asked if the installation of thermal insulation have benefits
Thanks again
Ariel