I've got a similar newcomer's problem to the "can't control temp fluctions" thread, although with a different sort of pot-still. I'm using an external heating element, simmerstat-controlled, and an air-cooled condenser scrounged off the back of a refrigerator - about 20m of 6-7 mm copper pipe. The brew is a honey-fruit wine that went oxidised, for what that's worth. Theory says this condenser should be good for 800W or so, more if a combination of wet sheet and fan is employed.
My problem is that I either get foaming and run-away temperatures of 92C in the still head, or no product. All the obvious problems can be ruled out - the temperature controller is as fine as you could want it to be, it doesn't matter how full the boiler is (a 20L thin metal drum), and the wash doesn't seem to be anything exceptional. Previous experience with smaller-scale Liebig-based systems worked as advertised, ie, the temp rose to 78C and then just stayed there, so up till now I was inclined to blame the condenser. The foaming is the part that I wasn't expecting - my preconceptions were that if the condenser wasn't up to the job then it would result in vapour coming out the end, not wash.
What I am mainly wanting to do at this point is get my head around the theory of why the rig is behaving as it is. If I have to, I will go water-cooled, but before I do that I want to know why I'm having to do that.
I guess I'm a little reluctant to part with the air-cooled principle, so the next move could be to use wider pipe (13mm) of a similar length. At this point, another theoretical question presents itself: would there be any advantage in inverting the condenser with the outlet to the high side, and a take-off valve near the still head? In other words, it would be a pseudo LM design, albeit without the reflux column. My speculation at this point is that this could make the cutting out of the heads quite problematic, as the pool above the valve might not necessarily contain the most volatile substances initially. Actually, the other distinct possibility is that quite a bit of vapour might want to escape out the valve as well. On the other hand, if you take a look at Alex's Spiral Head Still at "http://groups.yahoo.com/group/Distillers/files/Air Cooled.doc", this principle is claimed to be successful for reflux stills, and you wouldn't think that would make much of a difference to the vapour escape issue. Comments?
