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...
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...