Gas Pipeline Blowdown - Semiemperical Model - Report No. 87-2
Based on SW Research Report calculations for the blowdown time and mass of gas vented to atmosphere to a piping system. Accurate to within a few percent.
Blowdown time is impacted through constricting valve changes from sonic (choked) flow to subsonic. This is because of the pressure ratio across the valve is unknown.
ππ (π)Β β Volume of individual pipes[ft3]
π·π (π)Β β Diameter of individual pipes[in]
π€π‘π (π)Β β Wall Thickness of individual pipes[in]
πΏπ (π)Β β Length of individual pipes[mi]
πΒ β Friction Factor(Sum of flow friction through all diameters of blowdown piping)
πΏΒ β Blowdown Pipe Length[ft]
ππΒ β Internal Diameter of Blowdown Pipe[in]
π΄πΒ β CrossβSectional Area of Choke[in2]
π·πΒ β Diameter of Choked Flow Point[in]
π΄πΒ β CrossβSectional Area of Blowdown Pipe[in2]
ππΒ β Internal Diameter of Blowdown Pipe[in]
π π΄Β β Ratio of Choked Flow Area to Pipe Flow Area
ππΒ β Coefficient of Blowdown Loss(Sum of loss forΒ π π΄/πππ)
ππ πΒ β Initial Subsonic Pressure[psi]
πππΒ β Initial Pressure[psi]
ππΒ β Final Pressure[psi]
ππΒ β Base Pressure[psi]
ππππ£πΒ β Average Sonic Pressure[psi]
ππ ππ£πΒ β Average Subsonic Pressure[psi]
From the SWRI β SIMPLIFIED BLOWDOWN CALCULATIONS FOR PRESSURIZED GAS SYSTEMS Technical Report you can find tables and equations to complete many of the remaining calculations in this module.
πΎΒ β Can be found in table I of the SWRI Technical report mentioned above.
π Β β Universal gas constant (ππΒ = 1545)divided by the molecular weightΒ ππ€