Pressure drop across a tube section - compressible flow

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SUMMARY

The discussion centers on calculating the pressure drop across a stainless steel tube section with a length of 10mm and a diameter of 5mm, carrying 500 standard liters per minute of Nitrogen gas (N2). The primary challenge is applying Bernoulli's compressible flow equation effectively, particularly in determining velocity from mass flow while accounting for density variations due to pressure changes. The user expresses difficulty in finding straightforward solutions and emphasizes the need for a clear approach to this fluid dynamics problem.

PREREQUISITES
  • Understanding of Bernoulli's compressible flow equation
  • Knowledge of fluid dynamics principles, particularly for gases
  • Familiarity with calculating Reynolds number
  • Basic concepts of mass flow rate and density variations in compressible fluids
NEXT STEPS
  • Research the application of Bernoulli's equation in compressible flow scenarios
  • Learn how to calculate the Reynolds number for gas flow
  • Investigate entrance effects in fluid flow through tubes
  • Explore methods for approximating pressure drop in short tube sections
USEFUL FOR

Engineers, fluid dynamics researchers, and students tackling problems related to compressible flow in piping systems will benefit from this discussion.

ChrisEffinSmi
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So, a coworker approached me today with a 'simple problem' to solve, looking to sanity-check a design choice.

Much to my dismay, I had no idea how to approach it. Worse, google had no straight-forward answers either, and any formulae I did find seemed circular.

This seems too simple to require CFD or the like, and I feel like an obvious approach should jump out of standard equations, but I've been fussing with it for half a day to no avail.

Even just a point in the right direction would be much appreciated.

1. Homework Statement

A stainless steel tube section of length L (say, 10mm) and diameter D (say 5mm) has 500 standard liters per minute of Nitrogen gas (N2) flowing through it (so a mass flow of ~0.01042 kilograms per second, if I did my math right). What is the pressure drop across this tube section?

Temperature change is unknown, so unless that can be calculated or approximated, I guess we can assume an isothermic process? (I would think very little temperature change could occur over so short a distance anyway, but what do I know, I can't even start this problem...).

Homework Equations


Bernoulli's compressible flow equation (simplified) seems like it would be useful here, but its application escapes me, particularly when trying to extract the velocity from mass flow (how can I divide out density when gas density changes with pressure?)

j0upo4.jpg

https://en.wikipedia.org/wiki/Bernoulli's_principle#Compressible_flow_in_fluid_dynamics

The Attempt at a Solution


I got nothin'. =[
 
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Are you sure the L/D is only 2? For a longer tube, the first step would be to calculate the Reynolds number for the flow. With a small L/D like that, one also needs to consider entrance effects.
 
Chestermiller said:
Are you sure the L/D is only 2? For a longer tube, the first step would be to calculate the Reynolds number for the flow. With a small L/D like that, one also needs to consider entrance effects.

Thanks for the rapid attention!

Unfortunately yes. In actuality it's a small tube fitting welded to a much larger pipe. At first I thought to approximate it as an orifice, but the feed's ID is the same as the fitting's, and the pipe it's welded to is sufficiently large to be considered as 'open to atmosphere'. I probably should have been more honest with the physical nature of the system, but I was trying to keep things simple.
 

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