kirkwarren
Petroleum
- Sep 18, 2007
- 6
We are in the "planning" phase and have rough numbers generated for flows on our pipeline segment however one question is being bandied about; at what point are you simply paying too much for each additional HP to generate additional volume's of flow. I have found numerous references to corrosion at high gas velocities and API references to max velocity etc however we have very clean gas and I am not concerned with this. Does anyone know if there is a reference to a max gas velocity (for efficiency or economics)in spacing of compressor stations?