Simulation Basis:
HYSYS version = V10
EOS = (Peng-Robinson)
PIPESIM version = 2012.4
Pipeline Correlation = OLGAS 2014
Pipeline Friction Factor = 1.0
Pipeline Roughness = 0.04572 mm
Pipeline Basis:
Lets say:
Pipeline elevation = 75 m
Pipeline length = 10 km
ID = 247.6 mm
Process Input Basis:
Departing pressure = 30 Barg
Assume other values (e.g. materials) are defaulted & coating is negligible for simplicity.
The pipeline service is fully liquid (10-15% oil and 75-80% water).
Three mass flowrates (input) were used:
A - Minimum flow during Year 2050
B - Maximum during Year 2030
C - Arbitrary value.
C will be >> than B.
Using the dP Friction calculation (Darcy-Weisbach formula), dP ~ v^2.
The results:
Input A produces dP = 6 Bar
Input B produces dP = 1 Bar
Input C produces dP = >1 Bar (lets say 4 Bar)
If you plot out the results and compare it with Darcy's formula, you'll see that there is a region whereby the pressure drop is not governed by friction, instead the pressure drop decreases as the flow increases (opposite of Darcy's eqn).
My question:
What other possible parameter is affecting decrease of pressure drop when mass flow rate is increased (which corresponds to an increase in velocity).
My theory:
Is it head loss due to the vertical risers? Due to the low flow, there is a high static head in the pipeline especially due to the vertical risers.
Let me know if someone needs a TLDR version or any additional info.
Hope someone could help me out.
Cheers,