Can a Wide Angle in a Diffuser Cause Total Pressure Loss and Affect Gas Flow?

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Discussion Overview

The discussion centers on the effects of a wide angle in a diffuser on gas flow, specifically regarding changes in velocity and pressure as gas transitions through a duct or pipe expansion section. Participants explore theoretical frameworks, equations, and conditions relevant to subsonic and compressible flow, while considering the implications of geometry on flow characteristics.

Discussion Character

  • Technical explanation
  • Mathematical reasoning
  • Debate/contested

Main Points Raised

  • One participant seeks a formula to determine the velocity, pressure, and density of gas exiting a diffuser based on the area ratio of entrance to exit.
  • Another participant suggests the use of the Steady Flow Energy equation from thermodynamics to relate various flow parameters, including enthalpy and density, while correcting an earlier equation regarding gas density.
  • A participant connects the discussion to Bernoulli's equation, modified for compressible flow, and emphasizes the need to apply these equations to find the relationship between area expansion and changes in velocity or pressure.
  • One participant notes that gravity can be ignored only if the mass flow rate entering and exiting the diffuser is at the same physical level, highlighting the importance of the datum line in the analysis.
  • Another participant mentions that while incompressible fluid flow can be modeled using Bernoulli’s equation, gas flow is more complex due to isentropic expansion, which must be accounted for.
  • A participant points out that if the diffuser angle is too wide, flow separation may occur, leading to total pressure loss and violating isentropic conditions, thus complicating the application of Bernoulli's principle.
  • One participant acknowledges that while the flow is currently subsonic, it may become supersonic in the future, noting the differing effects of diffusing and converging flows.

Areas of Agreement / Disagreement

Participants express multiple competing views regarding the application of different equations and principles to model gas flow in a diffuser. There is no consensus on the best approach or the implications of flow separation due to wide angles.

Contextual Notes

Participants discuss various assumptions, such as the neglect of gravity under certain conditions and the complexities introduced by compressible flow. The discussion reflects a range of mathematical and physical considerations that remain unresolved.

airrocket
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Change in gas velocity and pressure entering and exiting a duct or pipe expansion section (diffuser). Looking for a formula to determine velocity, pressure and density of a gas as it exits a duct or pipe diffuser section based on the entrance area to exit area ratio. Ambient temperature, subsonic, subcritical flow.
 
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Im pretty sure this has to do with the Steady Flow Energy equation from thermodynamics.

This equation can equate velocities, pressures, mass flow rates, heat input/output and work input/output, enthalpy's and physical changes in height.

for enthalpy use,
h = c(p) dt

For the density of the gas, assuming it is a perfect gas use
P(pressure)*Velocity=m(mass)*R*T(temp in kelvin)

where R=(Universal Gas constant = 8.315)/M ... (M is the molecular mass of the gas)
keep in mind the units of universal gas constant its in "k" or thousand

good luck
 
Sorry I've made a mistake ..

that second equation is meant to be

P * V(volume) = m R T

note that m /v is density so P/RT = density

hope that helps
 
Thanks for the tips and equations. Yes I believe that maybe correct also related to Bernoulli's "conservation energy equation only modified for compressible flow. Now I have to figure out how to apply them to solve for the ratio of area expansion to change in velocity or pressure. Gravity does not appear to be a factor so I can ignore it. Once I get one the rest should all follow.
 
airrocket said:
Thanks for the tips and equations. Yes I believe that maybe correct also related to Bernoulli's "conservation energy equation only modified for compressible flow. Now I have to figure out how to apply them to solve for the ratio of area expansion to change in velocity or pressure. Gravity does not appear to be a factor so I can ignore it. Once I get one the rest should all follow.

Gravity can only be ignored if u have a single datum line. This means that the mass flow rate coming into the diffuser is leaving it at the same physical level(height) with respect to a reference plane. If the datum line changes(ie. change in distance from reference plane to the centroid of the diffuser inlet/outlet) between input and output, gravity does become a factor in the steady flow energy equation.
 
Expansion of an incompressible fluid through a diffuser can be modeled as Ksum mentions, simply using Bernoulli’s equation (less the ideal gas equation). However, for a gas, it’s not quite so simple. The gas is expanding isentropically, so you have to account for this. See attached.
 

Attachments

Yes, for now the flow is subsonic yet above M.3 so it is compressible. In the future it maybe supersonic in which case as I see diffusing/converging have opposite effects. Sounds simple yet gets very complex. Appreciate the assistance very helpful seems to confirm what I was thinking.
 
If the angle is to wide the flow will separate and you will have a total pressure loss hence the flow is not isentropic anymore and bernoulli does not nessesarily aply anymore.
 

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