If one gets a liquid between products change in the volume should be huge. Huge enough to be equivalent of just removing the reactant from the mixture.
But you are definitely right SO3 is not necessarily a gas at STP, I missed that part. It is volatile enough I always think about it being a gas, but I just checked - its boiling point is 45°C and melting point 17°C. I thought they were at least 30 degrees lower.
Correct, but I was wondering about complexities such as:
(a) Say the initial mix is at 1 atm. The BP of SO
3is 45°C. But as soon as you start converting to SO3 & that liquifies, the Pressure drops (since gas phase moles reduce) but that means the BP of SO3 also reduces.
(b) Since this is a multi-component situation would we have to worry about dew points & bubble points instead of a sharp 45°C BP?
In any case, there must be one unambiguous P=fn(conversion) function (assume isothermal at 30°C & fixed volume container) but I'd love to work on trying to analytically / numerically evaluate what it is.
Might be a challenging problem.