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I assume these are not "insert" type WL SSCSSVs that are back-ups to failed SCSSVs. In my experience you have a dome charge type and a spring type valve. Both should be evaluated once a year (or as needed for drastic changes in flow) for changes in flow characteristics of the well. A...

Thanks but I wasn't sure a Mechanical Engineer would be looking under the Petroleum section of the forum.

mbeychok, Thanks, this has gotten me started. Your assumptions about standard temp is correct. One question: What constant or what value did you use to take into effect the gas being under 1000 psia of pressure to get your volume of 793 cu ft (at 60 deg F and 1000 psia)? You used the formula...

I can't find a gas flowline volume calculation anywhere. Does anyone have a quick and dirty method. I have flow rate 10mmcfd, pressure 1000 psi, standard temp, pipe ID 4", and length (9088 ft). I want to know how much gas is in this flowline while flowing. How much when I shut it in (on both...

I can't find a gas flowline volume calculation anywhere. Does anyone have a quick and dirty method. I have flow rate 10mmcfd, pressure 1000 psi, standard temp, pipe ID 4", and length (9088 ft). I want to know how much gas is in this flowline while flowing. How much when I shut it in (on both...