Hi all,
I need to calculate the pressure drop for a biogas pipeline. The biogas is produced from a digester plant, so will be saturated with moisture. I assume the moisture will condensate in the pipe run, and will add into the friction losses.
I looked up the Lockhart-Martinelli correlation for gas-liquid flow, which adds a correction factor (theta):
DeltaP_2phase = (theta^2) * DeltaP_gasonly
theta^2 = 1 + C/X + 1/X^2
X is the Lockhart-Martinelli parameter
X = sqrt (deltaP_liq / deltaP_gas)
1) To calculate the liquid pressure drop, how can i estimate the condensate phase velocity?
2) Is it possible to simplfiy, by estimating the correction factor? According to Copilot, 1.2 - 1.5 is a good ballpark...
Thanks,

FB





