IngGasP
Petroleum
- Mar 18, 2012
- 20
Hi!
We had a compressor with inlet pressure 14 barg to outlet one 45 barg(design) for feeding gas with(3.0 MM Sm3/d) to LPG plant. we were controlling the pressure in the unit by turboexpander control valve (Completly different from conventional pressure control valve).Now,we're planning to convert the function of this booster from feeding LPG plant to discharge to another unit where the pressure is about 32barg.
I am given to do calculations on this new situation. What would be the steps to do in order to perform a good calculations?
See attached caracteristic curve of this compressor
Greetings
We had a compressor with inlet pressure 14 barg to outlet one 45 barg(design) for feeding gas with(3.0 MM Sm3/d) to LPG plant. we were controlling the pressure in the unit by turboexpander control valve (Completly different from conventional pressure control valve).Now,we're planning to convert the function of this booster from feeding LPG plant to discharge to another unit where the pressure is about 32barg.
I am given to do calculations on this new situation. What would be the steps to do in order to perform a good calculations?
See attached caracteristic curve of this compressor
Greetings