gregoryia
Petroleum
- Oct 30, 2011
- 1
Hi, I am trying to draw the operating line for H2S in the DEA contactor. I am trying to use equilibrium data from Kohl and Nielsen (1997). I have attached a link to some solubility data for DEA.
Does anyone know how to go about this problem, Any help would be much appreciated.
Cheers
Greg
Does anyone know how to go about this problem, Any help would be much appreciated.
Cheers
Greg