After reading DAD300's thread on Condenser Controlled Column stills, I have settled on that variation of the VM design. I am a huge fan of the K.I.S.S. concept and it fits well in those parameters. While my heart was set on a 3", the added cost of copper has me settled on a 2" w/ Keg Boiler for getting my feet wet.
My question is regarding the fitting at the point of vapor take off. There are many possibilites but most use a T fitting of one variety or another. From what I have gathered so far here, any horizontal area at this point on the still can collect small amounts of distillate, which could contribute to smearing..... yes?
Keeping things as simple as possible, I was considering using a 2" 45 deg Sani Wye fitting instead of a 2" T. With the takeoff angled down, all I would need is a reducer, eliminating one fitting (Wye -> Reducer vs. T -> Elbow -> Reducer). At this point, I'm sure it would suffice just fine. Cost wise, it would be the same-ish because of the increase in cost of the Wye, but simplicity and less joints are my goals.
The question on theory is not whether it will work as a still, the question is will it improve/degrade still function in any way.
With the takeoff angle down, there would be no place for distillate to collect which should make cuts cleaner with less smearing... Correct???
Reflux should be unaffected or slightly less because the condensate in the horizontal portion of a VM still isn't really counted on for reflux or is it? With the Condensor Coil all the way down, the take off point should be effectively closed off, and anything that did get by during initial full reflux would be discarded anyway.
While I am intending to run it angled down, I also have a question about angling it up and if their would be any advantage to that. With it angled up, I would assume the reflux ratio would be slightly higher with all else being the equal because a certain percentage would fall out of vapor and be reintroduced to the column, is there an advantage/disadvantage? This variation would also leave less area for condensate to collect, decreasing smearing issues as above, but would add another fitting unless you could find a 2" - 1/2" Reducing elbow.
And now last but not least... Because the takeoff is essentially a mitered 45 degree joint, the area exposed to the column is greater than if at 90 deg. With a 2" pipe, you are adding about 1.5 sq inches to the area at the column with all gains in the verticle plane. Would that decrease the efficiency of the column to separate distillates because with all else being equal the column would be effectivly 1/2" shorter? And/Or, because of the extra height of the opening, would that allow a less pure distillate because vapor is being collected from a taller section of the column? Would it decrease the time for a stripping run any amount due to the slight funneling affect of the increased area??
Sorry for the ramblings
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