We have had a recent increase in the number of incidents involving damage to our gas line. Our ordinances allow us to charge negligent individuals for the gas losses, labor, parts and other incidentals. Up to now most of them were in the ballpark of about 5 to 20 Mcf. Now we have a situation involving a severed riser. The stats are , 25 psi main, 200' of 3/4" steel pipe service line from the tap and 26 hours of blowing gas. I am using the gas loss section in GasCalc 4.0 to calculate the total volume of gas lost. My problem is that when I try to use one of the following standard equations: IGT-improved, Panhandle, Weymouth, Spitzglass I get a significant variance on the flow rate. Can someone please advise which one should be used and why.