Pressure rate increase between two vessels

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generating pressure between vessels to check for structural integrity
I have to cylindrical vessels using air as a medium. I want to pressurise vessel one, release the pressure into vessel to and register a .525mbar pressure in vessel 2 - within .3s.

My understanding so far,
dp/dt = 175000 Pa/s required

P1V1/n1 = p2v2/n2
52500 * 0.088627484 * 0.0041846 = 52500 * 0.088627484 * 0.0041846

for me if I have the required pressure in the same volume, and release this within 0.3 seconds, then i will get the exact same pressure on the opposite side.
But, once the valve is opened, the volume essentially doubles.

would I double the volume on V2 but i don't want the final pressure in V2 to change

My aim is to generate the pressure on the bottom section and see if it remains structurally sound.

any help please?
 
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  • #2
Welcome, @j117 !

For structural test of recipients, use water and a pump rather than compressed air.
It is not safe to use any compressible gas.
 
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the test has to be air, it is to replicate a delayed ignition in gas appliances, all safety is taken care of. I used a small tube to fill, the rate was not fast enough as I need am immediate impact as would be experienced in real terms
 
  • #4
I don't see how the equations you posted are relevant.
I believe you're trying to apply the ideal gas equations.

Initially, everything is known
1696182239469.png


After the expansion, we can find the equilibrium state assuming some things
1696182258314.png


The final volume I assume is known.
Then, if no mass is lost ##m=constant## and the process is adiabatic ##Q=0## we can conclude the internal energy will be the same as in the beginning because there is no work coming out ##W=0##.
$$\Delta U = Q-W \rightarrow U_f-U_i=0 \rightarrow U_i = U_f$$
Since the internal energy is only a function of the temperature in ideal gases, then the temperature must be the same before and after the expansion.
$$U_i = U_f \rightarrow T_i=T_f$$
You can check this link for more information about that.
https://en.wikipedia.org/wiki/Joule_expansion

Anyway, if you want to know something like ##dp/dt## you will need to characterize so many things that I believe it's easier to just use CFD. The gas will accelerate through the valve and then collide with the chamber walls. Something similar to a water hammer. I'm not certain if the pressure on the walls could be at some instant higher than the equilibrium pressure it will end up reaching as time goes on because of the mentioned collision.

Maybe if you check more info about water hammers and their gaseous version you can find something that works for you. If that's the case, post it back. It'd be interesting to read.
 
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Thread is in Moderation...
 
  • #6
Lnewqban said:
Welcome, @j117 !

For structural test of recipients, use water and a pump rather than compressed air.
It is not safe to use any compressible gas.
j117 said:
the test has to be air, it is to replicate a delayed ignition in gas appliances, all safety is taken care of. I used a small tube to fill, the rate was not fast enough as I need am immediate impact as would be experienced in real terms
After Mentor review, this thread will remain closed per the "dangerous discussion" prohibition in the PF rules.

From the Mentor discussion about this thread:
Delayed ignition is a lot like a potato gun without the potato in that the temperatures and pressures are very similar. Peak pressure on the order of 35-40 PSI is a number that sticks in my mind, and is consistent with what I observed when I watched a friend firing tennis balls from a potato gun.

The larger concern is that a test with compressed air does not properly test the system. If I was running this testing, I would set it up for the worst delayed ignition possible, then program it to repeat until stopped. My passing criteria would be about 100,000 cycles with no catastrophic failures. Allowable failures, such as the flame sensor, would shut the system down.
 
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1. What causes the pressure rate to increase between two connected vessels?

The pressure rate increase between two connected vessels can be caused by several factors including a temperature rise in one of the vessels, the transfer of additional gas or fluid into one vessel, or a decrease in the volume of one of the vessels due to mechanical action or design. The pressure differential drives the movement of fluids or gases from higher to lower pressure areas, leading to a change in pressure rates.

2. How can the pressure rate increase be calculated between two vessels?

To calculate the pressure rate increase between two vessels, you need to know the initial pressures and volumes of both vessels, as well as the temperature and the properties of the gas or fluid (like density and compressibility). The ideal gas law (PV = nRT) can be applied if the fluid is a gas and behaves ideally. For non-ideal scenarios, other equations of state like the Van der Waals equation may be needed. Calculations often involve determining the final equilibrium state where the pressures in both vessels equalize.

3. What are the effects of a pressure rate increase on system safety?

An increase in pressure rate can pose several safety risks, including the potential for vessel rupture, leaks, or explosive failures if the pressure exceeds the design limits of the vessel. It is crucial to have appropriate pressure relief systems and regular maintenance checks to ensure the integrity and safe operation of the system. Monitoring and controlling the pressure rate are essential to prevent accidents and ensure the longevity of the equipment.

4. How does the connecting pipe or valve affect the pressure rate increase between two vessels?

The size, length, and type of the connecting pipe or valve significantly influence the rate and extent of pressure equalization between two vessels. A larger diameter pipe or a fully open valve allows for quicker pressure equalization, while a smaller or partially closed valve can restrict flow, causing a slower pressure rate increase. The material and condition of the connecting elements also play crucial roles in the dynamics of pressure changes.

5. What methods are used to control the pressure rate increase in an industrial setting?

In industrial settings, controlling the pressure rate increase is crucial for process stability and safety. Methods include using pressure relief valves, rupture disks, and safety valves to prevent excessive pressure buildup. Additionally, automated control systems can adjust flow rates, open or close valves, or activate pumps to manage pressure dynamically based on real-time data. Regular system audits and simulations also help in anticipating and mitigating rapid pressure changes.

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