Calculating CFM at 40 psi from 3.7 CFM @ 90 psi

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Discussion Overview

The discussion revolves around calculating the cubic feet per minute (CFM) output of an air compressor rated at 3.7 CFM at 90 psi, specifically seeking to determine the CFM at a lower pressure of 40 psi. The conversation includes theoretical considerations, practical implications, and various approaches to the calculation.

Discussion Character

  • Technical explanation
  • Mathematical reasoning
  • Debate/contested

Main Points Raised

  • One participant suggests that the CFM does not increase significantly at lower pressures for a reciprocating compressor, although it might increase slightly due to various factors.
  • Another participant proposes a rough calculation using Boyle's Law, estimating that the CFM could be slightly less than twice the volume when dropping the pressure from 90 psi to 40 psi.
  • A different perspective emphasizes that manufacturers provide a CFM rating based on displacement, indicating that the flow does not decrease much with lower discharge pressure unless inlet density changes significantly.
  • Some participants discuss the concept of "free air flow" versus CFM at specific pressures, noting that manufacturers often refer to the actual displacement rather than the flow at a given pressure.
  • One participant raises a question about whether the CFM value is taken as actual or standard, leading to further clarification on the distinction between actual CFM and standard CFM based on inlet conditions.
  • Another participant shares specifications from their compressors, highlighting the importance of RPM as a controlling factor for volume output.

Areas of Agreement / Disagreement

Participants express differing views on how CFM changes with pressure, with no consensus reached on the exact relationship or the best method for calculation. Some agree on the general principles of compressor operation, while others contest specific interpretations of CFM ratings.

Contextual Notes

Limitations include assumptions about compressor type, the impact of temperature on calculations, and the lack of specific RPM data in some contributions. The discussion also reflects varying interpretations of manufacturer specifications and the definitions of actual versus standard CFM.

jimff
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I have an air compressor rated for 3.7 cfm @ 90 psi. what would the cfm be @ 40 psi? Is there a simple formula I can use?
 
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I have to believe this is a recip, so CFM doesn't increase much at the lower pressure. Might go up a bit because of various factors but not much.
 
Carry on running at 90 PSI and drop the pressure down through a regulator to 40 PSI and you should get about (slightly less then) twice the volume after the regulator. Very very rough calculation using Boyles Law and assuming that the temperature doesn't alter much.
 
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jimff said:
I have an air compressor rated for 3.7 cfm @ 90 psi. what would the cfm be @ 40 psi? Is there a simple formula I can use?

You didn't provide rpm so I could not get the volume of the compressor.
The shade tree method I use would be,...Assume 14.7 psi atmosphere, divide that into 90 psi for a compression ratio of 6.122.
Divide 90 psi by 40 psi to get 2.25, then multiply by 3.7 cfm to get flow volume of 8.325 cfm at 40 psi.

I'm surprised by one answer above.

Ron
 
Manufacturers of compressors provide a CFM rating which denotes the displacement, nothing more. The inlet pressure for this application is assumed constant, so regardless of discharge pressure, the inlet density times CFM determines the flow. The primary factors that reduce this capacity are void volume (volume of gas left inside the cylinder at the end of a piston stroke) and the piston ring blowby which should both be relatively small contributors to the reduction in flow. Being this is assumed to be a constant displacement machine, the flow doesn't decrease much as discharge pressure drops. Only an increase/decrease in inlet density would cause a signficant change in flow rate.
 
Guess we said the same thing in different ways, so a free flow of air at no compression, will be 22.65 cfm at whatever rpm the 3.7 cfm@ 90 psi was taken.
 
Is the cfm value taken as actual or standard?
 
RonL said:
Guess we said the same thing in different ways, so a free flow of air at no compression, will be 22.65 cfm at whatever rpm the 3.7 cfm@ 90 psi was taken.
Hi Ron. I understand your interpretation, but that's not what is typically meant for the small air compressor market (or even fairly large air compressors). When manufacturers talk about CFM, they aren't referring to the CFM at 90 psi which is what I believe you're suggesting. They're referring to "free air flow" as it's sometimes called. That's basically just the actual displacement of the machine. If they quote the CFM at a higher pressure, the machine will generally have a higher flow at lower pressure, but that has to do with gas that's re-expanding and leakage past piston rings. For a machine with a free air flow of 3.7 CFM at 90 psig, it may increase to 4 or slightly more CFM at 40 psig, but that's because the machine loses capacity due to leakage and recycle (void volume) as discharge pressure is increased.

Here's an example of a recip compressor similar to the one I'm assuming is being referenced by the OP.
http://www.gastmfg.com/pdf/piston/specsht/6h6l.pdf

Note the graph of pressure versus free air flow near the bottom of the page. This is a 2 stage recip with a flow of about 3.5 CFM at 90 psig and 4.0 CFM at 40 psig.

Jobrag said:
Is the cfm value taken as actual or standard?
CFM is actual. The compressor actually displaces X CFM, so you have to determine SCFM by comparing to actual conditions. If the temperature and pressure of the air being drawn into the compressor is at standard conditions, then the compressor is compressing that amount of air in SCFM. So for the 3.7 CFM compressor taken as the example, if the air going into the compressor is at standard conditions the flow is 3.7 SCFM. So it doesn't matter what the discharge pressure is; if the inlet conditions are standard, the flow in CFM is also SCFM.

Manufacturers do this to 'cover their a**' so to speak. They are just giving the displacement, and it is up to the user to determine what the inlet density is. The CFM is not CFM at the discharge pressure (ie: it is not 3.7 CFM at 90 psig and 70 F) it is 3.7 CFM at inlet pressure and temperature.
 
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Thanks Q_Goest,
When is being wrong a good thing ?:frown: When it brings out an answer that helps in giving a better understanding for the question ask.:wink:
I went to my shop and looked at the specs of two compressors purchased for a project I have been working on (very slowly), they are as follows.

5 HP, Air Compressor Pump
Air delivery: 1050 RPM
15.1 CFM @ 40 PSI
13.5 CFM @ 90 PSI
12.3 CFM @ 115 PSI
145-PSI max.

I lost sight of the fact that RPM is the most controlling factor for volume.

Thanks
Ron
 

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