Volumetric flow rate of nitrogen through relieving pressure regulator

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SUMMARY

The discussion centers on calculating the volumetric flow rate of nitrogen upstream of a relieving pressure regulator in a 1/4" OD nitrogen line. The upstream conditions are 100 PSIG and 70°F, while downstream conditions are 80 PSIG and 70°F, with a downstream consumption of 4 L/min (0.91 SCFM). Participants suggest using Boyle's Law for isothermal expansion and emphasize the importance of considering the regulator's specifications and the non-ideal gas behavior, particularly the z-factor, to accurately determine the upstream flow rate.

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  • Understanding of Boyle's Law and isothermal processes
  • Familiarity with pressure regulators and their functions
  • Knowledge of gas properties, including the z-factor for non-ideal gases
  • Basic skills in fluid dynamics and material balance calculations
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Gnardude
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Volumetric flow rate of nitrogen through relieving pressure regulator
Hello all,

I'm having trouble figuring out the volumetric flow rate upstream of a relieving pressure regulator used on a 1/4" OD nitrogen line. Upstream of the regulator P=100 PSIG and T=70F, while downstream P=80 PSIG and T=70F with downstream consumption at q=4 L/min or 0.91 SCFM (at std. T=70F, P=14.7 psia). My thoughts are to use boyles law, P1V1=P2V2 (ideal gas law), to calculate the upstream flow rate, which would equal 3.2 LPM not taking into account the flow leaving through the vent, however, I'm not too sure if the pressure regulator would impact the flow in anyway. Does anyone have an idea of how to calculate the upstream flow or if my method is correct? I currently don't have the spec sheet for the regulator, so I'm negating the flow through the vent until I have it tomorrow.
 

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Hello @Gnardude, :welcome: !

Gnardude said:
I'm not too sure if the pressure regulator would impact the flow in anyway
That's often what it is used for !

If the vent flow can be neglected you can write a material balance and for isothermal expansion use Boyle.

Usually, though, a pressure regulator is treated as isenthalpic and the gas as non-ideal. Since the flow is small, I expect the correction is reasonably small too (do you agree @Chestermiller ?).

(PS what a horrible mixture of units !)
 
BvU said:
Hello @Gnardude, :welcome: !

That's often what it is used for !

If the vent flow can be neglected you can write a material balance and for isothermal expansion use Boyle.

Usually, though, a pressure regulator is treated as isenthalpic and the gas as non-ideal. Since the flow is small, I expect the correction is reasonably small too (do you agree @Chestermiller ?).

(PS what a horrible mixture of units !)
You know the mass flow rate from the problem statement 0.91 SCFM. You also know the upstream pressure and temperature, so, including the non-ideality using the z-factor, you can get the upstream density. The volume flow rate upstream is equal to the mass flow rate divided by the upstream density.
 
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Gnardude said:
...a relieving pressure regulator...

vent...pressure regulator,,,

I currently don't have the spec sheet for the regulator...
What's a "relieving pressure regulator"? A safety relief valve? If so, it should have a nameplate with its relief pressure and flow rate. Yes, I think we need to know the specs of that device/what exactly it is/is doing.
 
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