Shortly after building it I insulated my pot still. I knew that it would have some reflux ramifications, but I considered that these would be minor, and it was something quite unexpected and specific that bit me: the insulation of the column.
Firstly, I have a phase angle controller so my heat input is not the issue. I have a temperature probe right at the swan neck and, in fact, thank goodness I do because otherwise I wouldn't have been able to deduce the problem. The problem was that - at least when doing a spirit run - the temperature of the probe, and the liquid output of the still, would vary wildly. It could easily jump 30°C in two minutes, and then drop just as fast. Even heating the still more slowly didn't seem to help much, and led to it taking many hours to heat up (and it's only 10 litres!). This first graph illustrates the problem I'm talking about. While heating up, the temp (and spirit output) was just all over the place. The temps do gradually converge, but the fluctuations were unacceptably large (click to enlarge):
I measured these data points last night while I was sitting there doing a run, watching the still get up to temp, and trying to figure out what on earth was going on. Clearly the charge was heating up, racing up the column (reflected by a large temperature spike at the swan neck) and then cooling and retreating back into the boiler again (reflected by a large temperature dip). And this pattern continued on and on. The question was: why was the pot, column and lyne arm not just gradually and steadily heating up like they should?
At some point it hit me that the insulation, not of the pot but of the column, was almost certainly the culprit. Why? Because at the point where the insulation ends it presents a large discontinuity to the vapour right before the temperature probe/swan neck. My hypothesis is that the charge heats up enough for the vapour to reach the swan neck, but at the very point that it reaches the neck, the insulation disappears and the vapour suddenly finds a whole lot of cold[er] copper which is not heated up yet. This cold copper absorbs the heat in the vapour and condenses it again. The process then repeats. It wouldn't be so bad if this was happening a good distance before the swan neck, but unfortunately my ending the insulation right before the neck ensures that much of the vapour in those surges makes it over the neck and it gets condensed and smears my product.
So after a while of collecting data I thought I'd test this. I stopped distilling, let the still cool down for a while, removed the insulation from around the column, and started heating up again. And here were the results(click to enlarge):
The first thing to notice is that the temperature DOES still fluctuate a little when the still is warming up, but far, far, far less. Also, it only took about 40 minutes for the temp to stabilize at 79°C. So this proves that without that particular insulation around the column of my still, the still performs insanely better.
Conclusions:(and extrapolations)
1. Starting or ending insulation near the swan neck of a (pot) still is not a good idea.
2(a). More generally, any discontinuities in a still will lead to fluctuations internal to the still, while the still is not in equilibrium (while it is heating up or cooling down).
2(b). The fluctuations will be most marked near where the discontinuity exists.
2(c) From (a) and (b): If the discontinuity is near the swan neck, those fluctuations will now present themselves as external fluctuations in the form of fluctuating distillate output.
Discussion:
In my still, and in many others' there are often large discontinuities. For instance where the column meets the pot, the diameter of the still decreases markedly. Even without the insulation in this experiment my still still (lol) fluctuated a bit while heating up (see graph 2). However - and here is the important point behind 2(c) - because this discontinuity (the decrease in diameter) is a fair distance away from the neck of the still, these fluctuations did not present themselves as output fluctuations.
You can bet that if I now decided to cut the column of my still so that the swan neck was only a few inches above the boiler - in other words near the discontinuity; the diameter change - that the distillate output would fluctuate again. My suspicion is that if I modified my still so that the diameter decreases slowly - as it does in a scotch whisky still - that I would mitigate the temperature fluctuations even more (I DO intend to do this once I have Spin Forming of copper sussed).
In more general terms - and these will be well known to skilled pot stillers and designers - any discontinuity in a still is going to produce fluctuations.
However, in many instances these fluctuations might be completely manageable, and may not manifest as output fluctuations. Discontinuities might include: changes in heat input, abrupt changes in dimensions, thickness, insulation, changes in material (e.g. SS to copper).
The phenomenon that is the subject of this experiment may not present itself so obviously to other still designs. Compared to the size of the boiler, my still is designed to have a comparatively large diameter over the swan neck. This results in a large mass of metal that needs to be heated up by a comparatively small boiler. Stills with large boilers compared to their output columns may not have such disastrous problems.
But the main moral of this story is to keep discontinuities away from the swan neck! I welcome comments/corrections/criticisms etc.
Thanks for listening!
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