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To recap, I am going to start with a pot still to get the hang of things. I'd like to have my setup in the basement, so that I have access to water and a drain, can run regardless of the weather, and am not permanently relegated to the garage. For safety (and more precise control), this leads me to heating the boiler electrically. I scored a free 1/2 bbl keg to work with as a boiler, but I want a larger opening than 2" and some extra ports for electric heating elements so I may end up not using this free keg. As an alternative, the 50L keg offered by USA Labs looks like a good deal as its already kitted out with a 6" tri-clamp opening at the top and a 1.5" tri-clamp on the bottom/side. The 6" port will give me flexibility with respect to what size column/riser to use and make clean-up much easier, while the 1.5" port can be used for a 5500W ULWD element or as a drain during cleaning. Ideally I'd have two more 1.5" tri-clamp ports along the side, one as a dedicated drain port and one for a thermometer or sight glass. If I really want to, I can seek out a TIG welder to help with those mods, but they're certainly not needed at the outset. As mentioned, I plan to use a 5500W ULWD heating element. To control the current flowing to the heating element, I'm looking at this triac kit offered by StillDragon (https://stilldragon.com/diy-controller-kit.html). It would also be nice to have a 1/6 bbl pony keg (7.75 gal) for smaller scale distillation, such as a second distillation of a stripped run.
I want a modular system for ease of cleaning, expandability, and ability to break down and store the still if it won't be used for extended periods. I scored some relatively inexpensive Cu pipe from a plumbing operation that was shutting down. I bought more than I needed because it was priced like 50% lower than retail, but I will actually use a mix of copper pipe and stainless steel tri-clamp fittings. I plan to go with a 2' riser made of 3" diameter copper tube to which I will solder 3" stainless steel tri-clamp ferrules at both ends. I'll throw some packing in the column (copper mesh or spiral prismatic packing) for neutral runs. [Question: do most people run their pot distillations of flavored spirits without any packing in the riser?] The riser will then meet with a tri-clamp (TC) conical reducer (3" to 2"), then to a 2" in-line sight glass (for some visual stimulus), and on to TC Tee fitting (2",2",2"). The top of the tee will be fitted with an end cap reducer and thermometer, and the side of the tee will go to a 2" TC 45-degree elbow. The elbow will mate to another TC reducer (2" to 1"), and then on to a copper Liebig condenser. I'll have to solder a 1" TC ferrule to the input end of the Liebig, and then if the Liebig inner tube is 3/4" then I'll also need a copper reducer (1" to 3/4") to transition from the TC ferrule to the input tube. I expect that the Liebig will be 36" in length. [Question: Is it overkill to have a Liebig with a 1" OD inner tuber/1.5" OD outer tube? Would a 3/4" OD inner tube/1" outer tube be sufficient or more appropriate, noting again that this will be a 50L (13.3 gal) pot still heated with a 5500W element?]
For cooling, I don't want to just run tap water, as that seems wasteful and possibly expensive, so I figure I will run a closed loop cooling system. This will consist of a large HDPE barrel (30 gal or 55 gal) to hold the water, and either a submersible pump or in-line pump to drive the water from the barrel through the condenser and back again. I ran some numbers estimating heat transfer in a typical 10 gal run, and it looks like 25 gal of water should be sufficient for pot stilling. This cooling setup will likely not be sufficient for refluxing though. Fractioning with a reflux setup would require a way to remove thermal energy from the coolant water (a project for another day). I would like to keep the coolant water potable, so that it can be used as a backup water source in case of emergency. This is simple enough, since I can get a food grade HDPE barrel, food-grade reinforced nylon tubing, and use lead free brass fittings for the coolant connections. Only catch is finding an appropriate pump that doesn't break the bank. [Question: any recommendations for inexpensive pumps that fit the bill?] I guess I could just go with a pond pump (not technically food safe) and just assume that if I'm having to break into my still coolant water for emergency drinking, there's probably bigger problems in the world than whatever impurities the pump may have introduced. i would also expect to grain and replace the coolant water every now and again to keep it potable, maybe some water purification tablets or something.
In any case, sorry for the long rant. I've included cartoon pictures of the proposed still, an exploded view that shows it broken down into components (excluding the heating and cooling portions), and the heat transfer numbers I ran.
Shout at me if you think I've gone off the rails or if I missed anything.
-V
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Water + Ethanol Distillation
Q=c*m*ΔT
Water
Enthalpy of Vaporization: 40.66 kJ/mol
Density (@RT): 1.00 g/mL
volume conversion: 0.264 gal/L
Specific Heat Capacity: 4.19 J/(°C g)
Ethanol
Enthalpy of Vaporization: 38.56 kJ/mol
Density (@RT): 0.789 g/mL
volume conversion: 0.264 gal/L
Specific Heat Capacity: 2.46 J/(°C g)
Hypothetical Distillation Run
ABV of Wash: 15 % (v/v)
Volume of Wash: 10 gal
Available Ethanol: 1.5 gal
ABV of distillate: 60 % (v/v)
How Much Distillate, if complete recovery of EtOH: 2.5 gal
Mass collected, Water: 3.78 kg
Mass collected, Ethanol 4.48 kg
Duration of Distillate Collection: 4.00 h
Water
ΔHdistill: 8,539 kJ
Power input to boil: 0.593 kW
Power input to coolant 0.593 kW
Ethanol
ΔHdistill: 3,752 kJ
Power input to boil: 1.758 kW
Power, input to coolant: 1.758 kW
Total power input to coolant: 2.351 kW
Volume of cooling water: 25 gal
Mass of water: 95 kg
Temp change of cooling water: 31.1 °C