We are calculating forces around piping and have some problems with the initial flow development.
Does anyone have experience with the the flows and flow dynamics in a piping system with the initial surge of flow. Our situation is natural gas at 1440 PSIG venting through a two inch full port valve to a vent stack.
I understand what is happening after the flow is developed with a standing shock wave somewhere at end or change in diameter.
What happens during the time between no flow and fully developed flow? I understand that an expansion wave travels upstream to the source and a travelling shock wave travels downstream to the end.
Maybe the question is can we open a 2" valve fast enough to create a shock tube effect?
Is this a way to get supersonic flow for a short time without a converging diverging nozzle? How would it revert back to sonic flow?
Thank you,
Paddler