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Pressure drop across a tube section - compressible flow

  1. Feb 23, 2017 #1
    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. The problem statement, all variables and given/known data

    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...).

    2. Relevant 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

    3. The attempt at a solution
    I got nothin'. =[
     
  2. jcsd
  3. Feb 23, 2017 #2
    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.
     
  4. Feb 23, 2017 #3
    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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