Dear All
In a gas sweetning unit the Lean rich exchanger of plate type is planning to change to shell and tube exchanger because of frequent choking in the previous one. I have the total simualted data of this unit.From this how can I go forward with the sizing calculation of this exchanger...
I have a sour gas mixture of 140mmscfd operating conditions are 75K and 1050psi.Does it means that at this condition the volume is 140mmscfd or at standard conditions. If in standard condition what is the temp and pressure. If I have to find the density of a particular gas say H2S what is the...
I have a doubt on the stochiometric calculation of a combustion reaction of H2S only. My feed is described in scfm. So is it correct if I consider scfm%=mol%, in the feed for my further calculation. I am eagarly waiting for your reply