pipelinevzla
Mechanical
- Feb 18, 2009
- 6
Greetings to all.
I would like someone to clarify whether from the standpoint of processes can be used with a valve JT effect for the following process:
The gas that comes from dehydration (0.5 lb / MM) is cooled in two stages (30 to 120 º F, 30 to 5 º F), then goes to a separator. The current ceiling for the sale of gas compressors to 1120 psi. Liquids can stop them through a JT valve and expanded to 350 psi and into a tower and Desetanizadora stabilization? or it would be through control valves?.
The top of the tower off gas recompression and mixing with residual gas. The bottom goes to LGN Fraccionamiento.
My question stems from the fact that I have always viewed JT valves in gas. No liquids.
thanks
I would like someone to clarify whether from the standpoint of processes can be used with a valve JT effect for the following process:
The gas that comes from dehydration (0.5 lb / MM) is cooled in two stages (30 to 120 º F, 30 to 5 º F), then goes to a separator. The current ceiling for the sale of gas compressors to 1120 psi. Liquids can stop them through a JT valve and expanded to 350 psi and into a tower and Desetanizadora stabilization? or it would be through control valves?.
The top of the tower off gas recompression and mixing with residual gas. The bottom goes to LGN Fraccionamiento.
My question stems from the fact that I have always viewed JT valves in gas. No liquids.
thanks