Relationship between Pressure and volume with Air

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Discussion Overview

The discussion revolves around the relationship between pressure and volume in a system where air is being pumped into a box at a specific flow rate. Participants explore the implications of Boyle's Law, the changing number of moles of gas, and the necessary parameters for calculating pressure, including temperature and density of air. The context includes both theoretical considerations and practical measurements.

Discussion Character

  • Exploratory
  • Technical explanation
  • Debate/contested
  • Mathematical reasoning

Main Points Raised

  • One participant questions the application of Boyle's Law to their scenario, suggesting that the results seem incorrect.
  • Another participant emphasizes the importance of specifying temperature, proposing a value of 310K for the discussion.
  • Concerns are raised about the changing number of moles of gas in the box over time, with one participant suggesting this is due to the mass of air entering being greater than that leaving.
  • There is a discussion about the need for the inlet density of air to determine the mass flow rate, with one participant providing a density value of 0.069 pound/ft².
  • A mathematical model is proposed to relate pressure, volume, and flow rates, leading to a steady-state pressure calculation of 196.7 kPa or 28.5 psi under certain assumptions.
  • Some participants express confusion about the calculations and seek clarification on how to apply the formulas correctly.
  • One participant acknowledges the complexity of the problem and suggests that the original post may be underspecified.

Areas of Agreement / Disagreement

Participants express differing views on the implications of air volume versus mass flow rates, and whether a steady state can be assumed. There is no consensus on the correct approach to the problem, and multiple competing views remain throughout the discussion.

Contextual Notes

The discussion highlights limitations such as the dependence on specific assumptions about temperature, density, and the nature of the flow rates. The mathematical steps and relationships among variables are not fully resolved, leaving some uncertainty in the calculations.

Who May Find This Useful

Individuals interested in fluid dynamics, thermodynamics, and practical applications of gas laws may find this discussion relevant, particularly those exploring the complexities of pressure calculations in dynamic systems.

teknicalissue
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Hey guys!

So the below question might sound like a homework question but in reality it is an oversimplified explanation of what I'm trying to measure

Let's say we have a perfect machine that pushes out 600CFM into a box. On the other end of the box is another small machine that only consumes 300CFM from the box.

What is the pressure in the box? and how do I calculate that? I've looked into Boyles Law and something just doesn't seem right about the results I'm getting so I'm trying to make sure that this is the right law I should be looking into.

If you need area of the box then let's assume it is 360in3

Thanks for lending a hand!
 
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teknicalissue said:
Hey guys!

So the below question might sound like a homework question but in reality it is an oversimplified explanation of what I'm trying to measure

Let's say we have a perfect machine that pushes out 600CFM into a box. On the other end of the box is another small machine that only consumes 300CFM from the box.

What is the pressure in the box? and how do I calculate that? I've looked into Boyles Law and something just doesn't seem right about the results I'm getting so I'm trying to make sure that this is the right law I should be looking into.

If you need area of the box then let's assume it is 360in3

Thanks for lending a hand!
You will have to mention the temperature as well.
 
benny_91 said:
You will have to mention the temperature as well.
For the sake of this experiment let's assume 310K
 
You are aware that the number of moles of gas in the box is changing with time, correct?
 
Hello,

This is a relatively new concept for me so I apologize if I don't understand something. I did not know that the moles of gas would change in time, is this because of the temperature increase that occurs over time? I'm trying to find a good example of how I can measure this so does this mean I would have to provide time? How about we say that this system is running for 5 seconds straight.
 
teknicalissue said:
Hello,

This is a relatively new concept for me so I apologize if I don't understand something. I did not know that the moles of gas would change in time, is this because of the temperature increase that occurs over time?
No. It is because more mass of air is entering than leaving.
I'm trying to find a good example of how I can measure this so does this mean I would have to provide time? How about we say that this system is running for 5 seconds straight.
You're missing much more important information than that. If you don't specify the inlet density of the air, we can't determine the rate of air mass entering. Giving the CFM of air does not specify the mass flow rate.
 
For the density of air, let's use 0.069 pound/ft2 of air.

Thanks again!
 
OK. Let's assume that the temperature is constant at 70 F. Then, if p is the pressure in the tank (psi), the number of lb-moles of air in the tank at any time is:
$$m=\frac{pV}{RT}$$where V is the volume of the tank (ft^3), T = 491.7 +70 = 561.7 Rankine, and R is the universal gas constant (10.73 ##\frac{psi\ ft^3}{R\ lb_{mole} }##). The rate of air entering the tank is 41.4 ##lb_m/min##=1.43 ##lb_{mole}/min##. The molar density of the air in the tank is m/V. The rate at which moles of air exit the tank is 300 m/V. So, from a mass balance on the air in the tank, $$\frac{dm}{dt}=1.43-300m/V$$, where t is measured in minutes. So, just solve this differential equation for the moles as a function of time, and then calculate the corresponding pressure.
 
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Thank you for your help!
 
  • #10
Chestermiller said:
You are aware that the number of moles of gas in the box is changing with time, correct?

Chestermiller said:
No. It is because more mass of air is entering than leaving.

I kind of disagree with that. The problem states that more volume of air is entering than leaving, not mass. Therefore we should assume that a steady state will be reached where ##\dot{m}_{in} =\dot{m}_{out}##, or:
[tex]\rho_{in}\dot{V}_{in} = \rho_{box}\dot{V}_{out}[/tex]
And if we assume that the temperature within the box is maintain to a pre-determined value, then:
[tex]p_{box} = \rho_{box}RT_{box} = \rho_{in}\frac{\dot{V}_{in}}{\dot{V}_{out}}RT_{box}[/tex]
With the given data (0.069 lb/ft³ = 1.1053 kg/m³; 600 CFM; 300 CFM; 287 J/kg/K; 310 K), we get a steady-state pressure of 196.7 kPa or 28.5 psi.

Of course, this can become more complex if we assume different conditions, such as no heat input/output from the box (so we have to find the final temperature within the box).
 
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  • #11
I thought about this too but as I said before I'm not expert. I think this is right on the dot on what I'm looking for. Thank you for replying!

@jack action Can you help me understand the formula a little better? as I said before, this is not a school thing and I'm trying the best I can to remember (and research) this.

To be more specific, how would you order the variables to equate 28.5 PSI? I know you provided the formula but I am unable to connect the variables to it.

Maybe something like:

P=14.7
T=344K

Etc etc
 
Last edited:
  • #12
jack action said:
I kind of disagree with that. The problem states that more volume of air is entering than leaving, not mass. Therefore we should assume that a steady state will be reached where ##\dot{m}_{in} =\dot{m}_{out}##, or:
[tex]\rho_{in}\dot{V}_{in} = \rho_{box}\dot{V}_{out}[/tex]
And if we assume that the temperature within the box is maintain to a pre-determined value, then:
[tex]p_{box} = \rho_{box}RT_{box} = \rho_{in}\frac{\dot{V}_{in}}{\dot{V}_{out}}RT_{box}[/tex]
With the given data (0.069 lb/ft³ = 1.1053 kg/m³; 600 CFM; 300 CFM; 287 J/kg/K; 310 K), we get a steady-state pressure of 196.7 kPa or 28.5 psi.

Of course, this can become more complex if we assume different conditions, such as no heat input/output from the box (so we have to find the final temperature within the box).
This sounds reasonable, but, of course, as you said, it all depends on the energy balance. My original impression was that this system is significantly underspecified by the OP. That impression hasn't changed.
 
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  • #13
teknicalissue said:
To be more specific, how would you order the variables to equate 28.5 PSI?
##\rho_{in}## = 1.1053 kg/m³;
##\dot{V}_{in}## = 600 CFM;
##\dot{V}_{out}## = 300 CFM;
##R## = 287 J/kg/K;
##T_{box}## = 310 K;
Putting those numbers in the equation gives ##p_{box}## = 196 677.082 Pa which you can convert to 196.7 kPa by dividing it by 1000 or to 28.5 psi by dividing it by 6894.757.
 
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  • #14
jack action said:
##\rho_{in}## = 1.1053 kg/m³;
##\dot{V}_{in}## = 600 CFM;
##\dot{V}_{out}## = 300 CFM;
##R## = 287 J/kg/K;
##T_{box}## = 310 K;
Putting those numbers in the equation gives ##p_{box}## = 196 677.082 Pa which you can convert to 196.7 kPa by dividing it by 1000 or to 28.5 psi by dividing it by 6894.757.

You rock! Thank you so much for this!
 
  • #15
@jack action

So I'm trying to plug the numbers in but I might be missing something. Can you check my math below?

X = ρbox * 287 * 310 = 1.1053* (600/300) * 287 * 310

Where do you find the value for ρbox?

Sorry for being so dense.. It's really embarrassing on how much of this stuff I've forgotten!
 
  • #16
Nevermind! I was able to figure it out!
 

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