Anybody with understanding of how Air pressure regulators function?

AI Thread Summary
Understanding air pressure regulators involves recognizing the relationship between CFM (cubic feet per minute) and PSI (pounds per square inch). Regulators control output pressure by balancing forces, typically using a spring mechanism, but the flow rate can also be influenced by the diameter of the air line. A larger diameter line can facilitate higher flow rates, but the actual flow will depend on the pressure differential across the regulator and the specific model's flow characteristics. The amount of air that can flow through a pipe is determined by the delta P (pressure difference) and the pipe's size, with no universal formula applicable to all scenarios. To effectively manage both flow rate and pressure, one must consider these variables and consult specific engineering data for the equipment in use.
Mattsnooze
Messages
15
Reaction score
0
As title dipicts I'm wishing to understand the relationships between CFM and PSI in regards to Air Regulation.

For example let's say I had a compressor tank with a compressor connected to it, to fill it to 200 PSI. I connect an X diameter Air line to an air regulator, and than have its output just an open X diameter Air line.

So my question is how can I control both variables. How could I have let's say a high flow rate, but lower maintained pressure. Or vice or versa, how could I have a low flow but at high pressure.

What I understand is that an air regulator (by some means) reduces the air pressure (PSI) by having a preset (spring rate) spring that opens after what ever you set the pressure tension bolt at(or what ever means the system uses to change spring reaction/travel). What I don't see is if the CFM would change based on what PSI the regulator is at. Also another thing I don't understand is how the X diameter line falls into play. I would think the larger the line, the higher the flow. Pressure would be the same but the tank would empty faster. How can I understand this fine line and learn how to balance those numbers.

Hypothetically let's say I know how much CFM I would like to generate, and I know at what PSI I want the CFM to be at. So in the end how would I control both those variables.

Hopefully me spelling it all out will avoid missunderstandings and replies that wouldn't hit the nail on the head and end up not giving me the exact answers or where to look for them.

Thanks for all those who read this short "story" and also to those who may reply!
matt
 
Engineering news on Phys.org
Regulators operate on a balance of forces combined with a particular flow geometry. Whether that includes a spring or a compressed air volume doesn't matter.

Here's a pretty good paper describing the theory:
http://www.samson.de/pdf_en/l202en.pdf
 
Excellent, thanks! That covered most of what I needed to know about the pressure regulators. I didn't end up seeing anything about how that changes how much air is flowed. It limits the pressure of the air comming out, so wouldn't that also mean the amount of air flowed would be substaintially less? Or because its compressed air, if its let out at 8psi, it will expand to a volume based on the compression level of 8psi?

Does anybody have any info on ways of compairing how CFM and PSI react with varrying sizes/diameter of piping or lines? For example, If I had a 1/2 inch diameter line, how much CFM could I flow through it. Also, how does the pressure its compressed at factor into this.
 
The amount that you can flow through a given pipe/opening will be totally dependent on the delta P across the thing you're flowing through. In the case of a regulator, you have to look at the specific model's engineering data to see the flow characteristics. There is no one set way that handles all different models.

This does not hold true for pipe flows though. If you do a search on this topic, there are a number of posts by Q_Goest in which he has posted a PDF of some very well known flow calculations.
 
Hi all, I have a question. So from the derivation of the Isentropic process relationship PV^gamma = constant, there is a step dW = PdV, which can only be said for quasi-equilibrium (or reversible) processes. As such I believe PV^gamma = constant (and the family of equations) should not be applicable to just adiabatic processes? Ie, it should be applicable only for adiabatic + reversible = isentropic processes? However, I've seen couple of online notes/books, and...
Thread 'How can I find the cleanout for my building drain?'
I am a long distance truck driver, but I recently completed a plumbing program with Stratford Career Institute. In the chapter of my textbook Repairing DWV Systems, the author says that if there is a clog in the building drain, one can clear out the clog by using a snake augur or maybe some other type of tool into the cleanout for the building drain. The author said that the cleanout for the building drain is usually near the stack. I live in a duplex townhouse. Just out of curiosity, I...
Back
Top