Arman77
Chemical
- Jan 26, 2011
- 1
Hi guys,
I am working on a project in the NGL plant and trying to calculate the leakge rate via a vlave, the upstream fluid is liquid with some associated vapour fraction.
I have the final leakage test pressure data after 45min of test.
also downstream volume in known and is fixed.
question is as liquid is passing through the valve it is flashing and making two phase mixture,therfore liquid by the time is compressing the vapour and pressure increases.
I want to know how to calculate leakage rate(both for the liq and gas mixture) under this condition? is still ideal gas law applicable?
any idea?
thanks
Mark
I am working on a project in the NGL plant and trying to calculate the leakge rate via a vlave, the upstream fluid is liquid with some associated vapour fraction.
I have the final leakage test pressure data after 45min of test.
also downstream volume in known and is fixed.
question is as liquid is passing through the valve it is flashing and making two phase mixture,therfore liquid by the time is compressing the vapour and pressure increases.
I want to know how to calculate leakage rate(both for the liq and gas mixture) under this condition? is still ideal gas law applicable?
any idea?
thanks
Mark