Finding Density & Diameter at Inlet & Outlet

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Discussion Overview

The discussion revolves around calculating the density at the inlet and outlet, as well as determining the diameter at the outlet of a system involving gas flow. Participants explore the implications of pressure and temperature on density, the relationship between mass flow and area, and the geometry of turbine designs. The context includes technical reasoning and mathematical calculations related to fluid dynamics.

Discussion Character

  • Technical explanation
  • Mathematical reasoning
  • Debate/contested

Main Points Raised

  • One participant states that density can be calculated using the formula density = pressure/(RT), where R is the gas constant and T is the temperature.
  • Another participant points out a discrepancy in the problem regarding the inlet pressure, noting that the diagram shows 160 psi while the problem states 45 psi at the outlet.
  • Some participants agree that heat loss does not affect the density or diameter calculations.
  • There is a discussion about the assumption that turbines have circular cross sections, with one participant suggesting that round shapes are preferred due to ease of machining and reduced thermal stress.
  • Several participants express confusion over the calculated outlet area, with one participant noting that their result was smaller than the inlet area, while others report larger exit areas.
  • One participant mentions that their calculations yield a diameter of 0.453 ft, while another participant calculates an area of approximately 0.16 ft².
  • There is a mention of the conservation of mass principle, with participants discussing the relationship between density, area, and velocity in the context of fluid flow.

Areas of Agreement / Disagreement

Participants generally agree on the method for calculating density and the implications of heat loss, but there are multiple competing views regarding the expected outlet area and the geometry of turbines. The discussion remains unresolved regarding the discrepancies in calculated areas and the implications of the problem's diagram.

Contextual Notes

Participants express uncertainty about the accuracy of the problem's parameters, particularly the inlet and outlet pressures, and the implications of these values on their calculations. There is also a lack of consensus on the expected relationship between inlet and outlet areas in turbine designs.

pyroknife
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I attached the file.

I just wanted to clarify something.

All i need to find is the density @ inlet&outlet and the diameter at the outlet.

The heat loss they have shown has no impact on the values that were asked for right?

density can be found by pressure/(RT) where R=gas constant and T=temperature
And the diameter can be found by setting the mass flow at the inlet = mass flow at the outlet.
 

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The problem states the inlet pressure is 45 psi. But the diagram shows 160 psi at inlet. The 45 psi is shown at the outlet. Something is amiss.

But to answer your question, if you know P and T, you can determine density. Knowing that you know the mass flow. The heat loss has no impact on the values asked. Conservation of mass will determine exit area.
 
Yeah I noticed that typo too. The prof said to assume it is 160 psi. Okay I thought so.

Basically my calculations for the density was pressure/(RT)
Where R=gas constant of air and T=temperature in rankineI just said set (density at inlet)*(Velocity at inlet)*(Area of inlet)=(density at outlet)*(Velocity at outlet)*(Area of outlet) and solved for the exit area.

But jst out of curiosity, all turbines have circular cross sections right?
 
A round shape is the easiest to machine and therefore costs less. Exhaust pipes are subject to thermal stresses due to piping wanting to expand radially and axially at startup. If it were square or had any corners, you would have built in 'stress risers' that would make it more prone to failure. Round is best for any number of reasons.
 
LawrenceC said:
A round shape is the easiest to machine and therefore costs less. Exhaust pipes are subject to thermal stresses due to piping wanting to expand radially and axially at startup. If it were square or had any corners, you would have built in 'stress risers' that would make it more prone to failure. Round is best for any number of reasons.

Oh okay, I just solved the problem, but something weird happened.

The way the picture is drawn, the outlet area should be bigger, but the area I got issmaller than the inlet.
 
Last edited:
Yes, I also end up with a larger exit area. But rho*A*V = constant. Working fluid is air. If you know pressure and temperature, you then know density. The trapezoid symbols used for compressors and turbines in thermo texts are meant to infer the working fluid is compressed or expanded. The numbers in this problem are strange.
 
LawrenceC said:
Yes, I also end up with a larger exit area. But rho*A*V = constant. Working fluid is air. If you know pressure and temperature, you then know density. The trapezoid symbols used for compressors and turbines in thermo texts are meant to infer the working fluid is compressed or expanded. The numbers in this problem are strange.

Thanks. did you get diameter = 0.453 ft?

I talked to a friend. He says turbines are supposed to have a smaller outlet area than inlet. And that the figure is drawn like a diffuser instead of a tirbine.
 
I do not calculate 0.453 ft^2. I get a little over 23 in^2 which is 0.16 ft^2.
 
First I calculated the two densities
At 1: density=P1/(RT1)
P1=(160 lb/in^2 * 12in^2 / 1ft^2)
R=(1716 ft*lbf/(slug*R)
T1=320+460 R
P1= .0172 slug/ft^3

P2=45 lb/in^2 * 12in^2/1ft^2
R=1716 ftlb/(slugR)
T2=50+460 R
Density 2=.0074 slug/ft^3

COnservation of mass:
(.0172)(30/144 ft^2)(100ft/s)=.0072 slug/ft^3 * 300 ft/s * A2
A2=.1614 ft^2
Diameter=.453 ft

Crap! I just wrote this all out for no reason. I meant I got diameter=.453 ft. I got Area=.16 ft^2 as well.
 

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