Anyone have any suggestions as to the best way to calculate the amount of shell side refrigerant that is pushed into the relief valve during a tube rupture relief scenario in a heat exchanger? The tube side is gasoline and I've calculated the flowrate based on flow thru both ends of an orifice...
I am trying to find the minimum flow rate for a set of Sour Water Pumps that have been in existence for some time in the refinery. I have two pump curves. One is the performance curve from the vendor which shows various impeller sizes, hp, etc.. and the second is a characteristic / test curve...
