Volumetric flow rate of nitrogen through relieving pressure regulator

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Discussion Overview

The discussion revolves around calculating the volumetric flow rate of nitrogen upstream of a relieving pressure regulator in a specific setup involving pressure and temperature conditions. Participants explore the implications of using Boyle's law and the characteristics of the pressure regulator on flow calculations.

Discussion Character

  • Technical explanation
  • Debate/contested
  • Mathematical reasoning

Main Points Raised

  • One participant proposes using Boyle's law (P1V1=P2V2) to calculate the upstream flow rate, suggesting an initial estimate of 3.2 LPM without accounting for vent flow.
  • Another participant notes that the pressure regulator typically impacts flow and suggests writing a material balance for isothermal expansion while acknowledging the potential for non-ideal gas behavior.
  • A third participant emphasizes the importance of knowing the regulator's specifications, questioning whether it is a safety relief valve and highlighting the need for its nameplate data to understand its operation better.
  • There is mention of the mass flow rate being known (0.91 SCFM) and the possibility of calculating upstream density using the z-factor to determine the upstream volumetric flow rate.

Areas of Agreement / Disagreement

Participants express differing views on the impact of the pressure regulator on flow calculations and the necessity of its specifications. There is no consensus on the best approach to calculate the upstream flow rate, and the discussion remains unresolved.

Contextual Notes

Participants note the mixture of units used in the problem, which may complicate calculations. The discussion also highlights the uncertainty regarding the regulator's specifications and its effect on flow behavior.

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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