If you are doing static with heat transfer, then the vessel will try to heat the lifting tool, the thermal expansion of which is likely restrained as the base of the tool may be at a lower temperature. So this may introduce additional stress.
In case it is a priming arrangement, there should be a water connection with a valve at the top for refilling the pipe(priming tank) in case it gets drained due to leakage or backflow.
It introduces pressure drop as already been said. Which increases possibility of cavitation.
It introduces flow disturbances at suction increasing the propensity for cavitation again.
It provides a place for air to accumulate and thus may result in vapor lock and reduction of flow.
The flow velocity in 2 in header with a total 200 gpm flow is around 6 m/s, which is high. There will be a significant pressure drop in the header itself.
So, a thorough review of pipe sizes along with the pump head-capacity curve is required.
Version 1 is used generally.
Version-2 will give the same result as version-1 if the ideal gas cycle is used, as enthalpy depends on T only and not dependent of P.
If the actual gas cycle is used, then the normally used formulae for gas cycles can not be used any more, and enthalpy depends on...
First, you calculate the enthalpy at 7 bara saturated. Then do iterations to match the enthalpy at 1.37 bara by successively changing the temperature and getting the enthalpy from the software.
@Dulli2000
Thank you for letting the cat out at last!
1. If your PSV set pressure is above the saturation vapor pressure at the particular temperature inside the vessel, it is possible that relieving pressure will not be reached just when all the liquid has vaporized. Pressure will increase...
NFPA typically specifies an underground valve roadway box.
The indicated valve location will have difficulty in operation. However, the same may be as per AHJ clearance.
Regarding the coverage area of hydrants, it depends on local practice and AHJ.
Assuming you want the temperature at the outlet of PSV, where the pressure is 1.37 bar(a). The process is adiabatic(isenthalpic). Using the steam table software in Excel, the required temperature at the exit of PSV is 144.5 deg C.
You can try to use Sec VIII Div 3 which caters to high pressures. Even though piping is outside its scope, it is permitted to design as per this code and get a U3 stamp if necessary.
Even though formulae for stresses in thick walled cylinders are available, the complications will arise due to...