Please, if you happened to read it, disregard a previous post by me that I've deleted. There is a mistake in it.
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Update:
You assume that you have 3 componentes (isobutane, n-butane and propane)
Two phases
So for intensive properties you have:
F = C-P+2 = 3 degrees of freedom
Extensive variables add one more per phase that is, a total of 5 degrees of freedom.
You know:
- Pressure
- Temperature
- Total volume of Liquid
- Total volume of Gas.
You are missing one variable to be able to solve the system. You may assume a constant ratio of butanes (iso/normal), probably without making a big error (at least better than assuming a constant density).
But... you have the following difficulties:
- You assume that temperature is uniform. If the tank is not insulated and exposed to sun, this might not be true.
- The the tank is perfectly mixed and in equilibrium.
- There are no other components apart from propane, isobutane and normal butane. Small amoung of volatiles/non condensables will distort your pressure (ethane, methane, nitrogen)
If you really need a measurement of density, the best way is to purchase a ASTM D1657 hydrometer. The price is accesible even to a small operation if having an accurate inventory control is an issue.
Edited by Saml, 25 June 2018 - 06:57 PM.