Stuuus
Petroleum
- Jul 7, 2017
- 16
Hello,
I am currently making a calculations spreadsheet for pipeline services and am thinking of how best to calculate gas flowrates. Liquid is simply the Darcy-Weisbach equation with Churchill (Darcy) Friction Factors.
However when it comes to gas, for example the dewatering of a liquid-use pipeline precommissioning, I am considering using the general gas flow formula described in "A Tutorial on Pipe Flow Equations" - Schroeder.
Currently I have five pipeline sections programmable, and a downline (hose) each could be different lengths and diameters.
Is there some form of this equation which accounts for the different sections?
If not, then I am considering setting an equivalent diameter of say 10" for example, and calculating the required length of this 10" pipe to generate the same back pressure as the original diameter and length of pipe, with the same flow rate. With all sections translated into the equivalent length of 10" pipe, then using this to calculate the required parameter. Is this acceptable?
Pipeline Services Engineer in the Oil & Gas Sector
I am currently making a calculations spreadsheet for pipeline services and am thinking of how best to calculate gas flowrates. Liquid is simply the Darcy-Weisbach equation with Churchill (Darcy) Friction Factors.
However when it comes to gas, for example the dewatering of a liquid-use pipeline precommissioning, I am considering using the general gas flow formula described in "A Tutorial on Pipe Flow Equations" - Schroeder.
Currently I have five pipeline sections programmable, and a downline (hose) each could be different lengths and diameters.
Is there some form of this equation which accounts for the different sections?
If not, then I am considering setting an equivalent diameter of say 10" for example, and calculating the required length of this 10" pipe to generate the same back pressure as the original diameter and length of pipe, with the same flow rate. With all sections translated into the equivalent length of 10" pipe, then using this to calculate the required parameter. Is this acceptable?
Pipeline Services Engineer in the Oil & Gas Sector