mbsterli
Mechanical
- Feb 18, 2015
- 2
Hello all,
First post...
I'm assessing discharge piping of multiple liquid pressure relief valves installed on the downstream side of chemical metering pumps. Each is situated within ASME B31.1 Nonboiler External Piping. The relief valves each have a 1/2" MNPT inlet and 1" FNPT outlet, with a 'C' orifice (0.062 in2 orifice area). Currently the inlet piping to the relief valves is either 3/8" or 1/2". The discharge piping is either 3/8" or 1/2" leading back to the chemical storage tanks.
Section 122.6.2 of ASME B31.1 states that "Sectional areas of a discharge pipe shall not be less than the full area of the valve or device outlets discharging thereinto". My initial interpretation is that all discharge piping must be at least 1" in diameter (to match the 1" FNPT outlet). Is that correct? Or is the "full area of the valve" referring to the orifice area, in which the existing installation would be okay?
As the metering pumps provide such low flows (between 0.5 and 20 GPH), the existing piping is large enough as to not create excessive backpressure and inhibit the pressure relief. Should the piping be changed out anyways?
Thanks
First post...
I'm assessing discharge piping of multiple liquid pressure relief valves installed on the downstream side of chemical metering pumps. Each is situated within ASME B31.1 Nonboiler External Piping. The relief valves each have a 1/2" MNPT inlet and 1" FNPT outlet, with a 'C' orifice (0.062 in2 orifice area). Currently the inlet piping to the relief valves is either 3/8" or 1/2". The discharge piping is either 3/8" or 1/2" leading back to the chemical storage tanks.
Section 122.6.2 of ASME B31.1 states that "Sectional areas of a discharge pipe shall not be less than the full area of the valve or device outlets discharging thereinto". My initial interpretation is that all discharge piping must be at least 1" in diameter (to match the 1" FNPT outlet). Is that correct? Or is the "full area of the valve" referring to the orifice area, in which the existing installation would be okay?
As the metering pumps provide such low flows (between 0.5 and 20 GPH), the existing piping is large enough as to not create excessive backpressure and inhibit the pressure relief. Should the piping be changed out anyways?
Thanks