2phase
Geotechnical
- Nov 1, 2003
- 2
Dear participants!
I have a problem maintaining the estimated performance in a two phase pipeline transporting steam/liquid from a well to a power plant, due to a decisive slugflow in the pipe.
Illustration:
The pipe is horizontal, well temp. 240°, pipe pressure 6 bar (gauge), pipe diameter 406 mm (16”). The pipe is designed to transfer 10 kg/s of steam and 50 kg/s liquid (brine).
All tips for approaching the phenomena “slug flow” are appreciated
Sincerly, 2-phase
I have a problem maintaining the estimated performance in a two phase pipeline transporting steam/liquid from a well to a power plant, due to a decisive slugflow in the pipe.
Illustration:
The pipe is horizontal, well temp. 240°, pipe pressure 6 bar (gauge), pipe diameter 406 mm (16”). The pipe is designed to transfer 10 kg/s of steam and 50 kg/s liquid (brine).
All tips for approaching the phenomena “slug flow” are appreciated
Sincerly, 2-phase