Omid1977
Petroleum
- Mar 12, 2010
- 3
I am designing PSV for a fuel gas scrubber,
Governing case is gas blow-by through two pressure regulators (PCV)upstream fuel gas scrubber. Flow through these two valves is two-phase and gas and liquid are separated in fuel gas scrubber therefore I only considered gas portion of flow through regulators as my design relief load of PSV(is it true?).
Upstream pressure of PCV's considered 68barg and down stream pressure considered 17barg(set pressure of PSV on fuel gas scrubber) + 10%
I know that if both regulators fail(my design case for considering gas blow-by) generated gas flow rate will be less than rated flow rate of fuel gas PSV. But do I need to size line upstream this PSV according to Rated flow of PSV or Relief load (max possible flow during gas blow by) is sufficient ?
Governing case is gas blow-by through two pressure regulators (PCV)upstream fuel gas scrubber. Flow through these two valves is two-phase and gas and liquid are separated in fuel gas scrubber therefore I only considered gas portion of flow through regulators as my design relief load of PSV(is it true?).
Upstream pressure of PCV's considered 68barg and down stream pressure considered 17barg(set pressure of PSV on fuel gas scrubber) + 10%
I know that if both regulators fail(my design case for considering gas blow-by) generated gas flow rate will be less than rated flow rate of fuel gas PSV. But do I need to size line upstream this PSV according to Rated flow of PSV or Relief load (max possible flow during gas blow by) is sufficient ?