Can anybody show any random example for caclulating specific volume increase? I understand that Latexman has provided a thread for the formula, but I am confused about dv/dT term.
Hi everyone,
Recently I am working on thermal expansion case for relief valve design. System is HX with crude being heated by shell side other HC. Process fluid is crude (on tube side of HX) and PSV set value is 400 psig. I have considered tube rupture - not applicable, blocked out- not...
Hi everyone,
Recently I am working on thermal expansion case for relief valve design. System is HX with crude being heated by shell side other HC. Process fluid is crude (on tube side of HX) and PSV set value is 400 psig. I have considered tube rupture - not applicable, blocked out- not...