you’ll have to decide for yourself where you want to place the cutoff for “stop venting”, because there will always be some butane even if your tank is well below the boiling point.
…and I don’t recommend the “try setting it on fire” approach, despite having threatened such on numerous occasions.
Say you had butane at -50C in a tank pressurized
With N2 at 100 psi, let the system come to equilibrium. What makes you think the mole fraction of N2 in solution would be insignificant?
I.e., in regards to added vapor pressure if the system were allowed to re-equilibrate to room temp? N2 is non polar why wouldn’t it readily dissolve?
Someone should do this experiment in a Parr reactor with a 5000 psi gauge… I think you might be surprised.
Certainly the solubility at room temp is negligible…but that is the source of excess pressure hazard? I have seen a white butane tank split open in such a manner.
the easiest N2 implementation involves never actually emptying your solvent tank. that way the N2 never leaves that tank (only provides head pressure).
assuming you keep your solvent tank well below zero, you can vent to 0PSI (actually pull vac if you’ve cold enough and have the right tooling) before recovery.
with a thermocouple in the solvent tank, a scale, and sight glasses, I’ve looked at the above solution fairly extensively. the guidance I gave my crew was
a) use phase diagram. make sure you’re below boiling point of solvent mix.
b) use scale when venting. how much weight did you loose? aim for “none”.
c) watch the solvent. once it starts to bubble you’re venting solvent.
d) use the detector. calibrate it using the above.
I don’t have a real lab . I’m just some one using a little 1 pound cls on my front porch . But I’m trying to get my license for a lab next year so I’m in the process of trying to learn and perfect a system that I can then scale up for my future licensed lab . But I don’t see myself having the capital to pay anyone for professional help even once I get my license . But eventually if I get the money I can definitely see having a professional on staff being a huge help . That’s the goal , but seems like it’s years away at best . I definitely understand where ur coming from tho
you can certainly get most of the solvent out. either actively or passively. I’d prefer to save pumps for active column recovery only. haven’t had the opportunity to run that way yet.
you can get more out if you heat the columns.
or cool the collection.
if you want to push N2 all the way through to collection, you’re going to have to cool the collection to vent, or recover and then vent. that last option gets dangerous if you add pumps.
Absolutely true, AND, doesn’t make a huge difference when you’re playing with small volumes of butane in a non-production environment (I’ve played this with high propane blends, and it definitely slows recovery, just not enough that I’d be willing to use a rotary vane on it & the air-Venturi pump never showed )