TMDD
Chemical
- Mar 5, 2003
- 1
I am working in a refinery and I want to design a gas - liquid mixing point.
The gas is mainly C1, C2, C3, C4 and the liquid is mainly C3, C4.
Both gas and liquid lines are carbon steel.Gas line is 4 inches and liquid line 1 inch. The quantity of the gas is much higher than the liquid.Both streams are not corrosive.
I suppose that a simple carbon steel tee might not perform very well because there is a temperature differnce of 60 C (gas at 80 C and liquid at 20 C)
I am not aware if there are any considerations about special materials like Stainless steel or an internal sleeve.
Also I would like to help me on mechanical design issues (distances, drawings etc)
Does anyone know anything?
Thanks
Bil
The gas is mainly C1, C2, C3, C4 and the liquid is mainly C3, C4.
Both gas and liquid lines are carbon steel.Gas line is 4 inches and liquid line 1 inch. The quantity of the gas is much higher than the liquid.Both streams are not corrosive.
I suppose that a simple carbon steel tee might not perform very well because there is a temperature differnce of 60 C (gas at 80 C and liquid at 20 C)
I am not aware if there are any considerations about special materials like Stainless steel or an internal sleeve.
Also I would like to help me on mechanical design issues (distances, drawings etc)
Does anyone know anything?
Thanks
Bil