rb1957 looking at it another way... (as in a bubble of 0.0027in3 p/sec)
Converting: .00027 cubic inch into Psi - using Ideal Gas Law. All constant variables reduced.
P1V1 = P2V2
P2=P1V1/V2 = ((23.3) (1in3))/((.9973 in3)) - knowns (14.7+8.6 absolute pressure)
P2 = 23.36...
Meant to say...
"part (is NOT sealed hermitically). Not that it matters.... been a long day..
rb1957... I follow you on the atm, psig etc... but maybe im tired
I don't see how you derived at P = 56629 ?
Thanks for help by the way.
errr I keep getting pulled off this to do other things sorry.
n = 293*.0001782(Vm3) / 8.314*293.13
The part is communication amplifier device (is sealed but hermitically).
Hmmm, the vol leak rate (0.0027) is actually the max LR spec.
which I need to know in psi.
the PL of .008 psi is what the machine is capable of catching known fails at.
i'll review... thx rb1957
littlrich...
a chamber (alum box, with a unit in it) is filled with 8.6 psi for testing a unit (so 1 atm + 8.6), V in cc.
Pa absolute Pascal.
machine is fairly repeatable, again this was handed down to me.
not homework really,
have a pressure loss of .008 psi on a leak tester was told that it equated to 0.0027 cubic inch p/second but I need to prove this.
The people who originally set this up are no longer here and the Leak test company no longer in biz.
leak tester (provides external pressure...
Hmmm I only know the 0.0027 cubic inch p/second to psi p/second leakrate...
I don't know the atmospheric / temp conditions.
isn't there a more direct way to convert?