Weegie
Petroleum
- Feb 20, 2007
- 60
Looking for some guidance please on settings/calcs for air purging instrument impulse lines.
Situation is as follows.
Atmospheric Furnace (refinery)
Operating temp & pressure 1750 Deg F & 3.5psig
Max temp and pressure 2100 Deg F & 6 psig.
Refinery std is for a Fisher air regulator feeding air through
3/8"od tube via a 3/8" tubing union with a 0.125" in line restriction orifice and tee'd into the pressure transmitter impulse line.
Is there a rule of thumb as to how much higher the purge pressure is in relation to the prossess operating pressure ?
How would I calculate the flow rate and pressure drop due to the in line restriction orifice ?
Many thanks in advance.
Situation is as follows.
Atmospheric Furnace (refinery)
Operating temp & pressure 1750 Deg F & 3.5psig
Max temp and pressure 2100 Deg F & 6 psig.
Refinery std is for a Fisher air regulator feeding air through
3/8"od tube via a 3/8" tubing union with a 0.125" in line restriction orifice and tee'd into the pressure transmitter impulse line.
Is there a rule of thumb as to how much higher the purge pressure is in relation to the prossess operating pressure ?
How would I calculate the flow rate and pressure drop due to the in line restriction orifice ?
Many thanks in advance.