I’ve been tinkering with a similar design to heat the Hot Liquor Tank — and then be able swap the HLT as a still boiler to harvest the ethanol after fermentation ..for refining biodiesel...
...and making hand sanitizer [I swear.]
Kinda following-up on Glenn’s reply...Depending on the construction of the pot you’re using for your HLT, the flue gasses could still be an issue with scaling ...like if your pot has a 3-ply bottom (2 layers of stainless steel with aluminum sandwiched between)
Even with water in the pot, the center will be intensely hot right above the riser, and that might damage a tri-ply sandwiched pot bottom... or warp and begin to corrode a single-layer stainless pot.
From AZOM materials fact sheet on 304 stainless (the grade used in almost all stainless cookware and most brewing equipment):
> “...grade 304 stainless steel possesses “good oxidation resistance in intermittent service to 870 °C and in continuous service to 925 °C.” However, they warn that “continuous use of 304 in the 425-860 °C range is not recommended if subsequent aqueous corrosion resistance is important.”
> 304H will become sensitized in the temperature range of 425-860 °C. Whilst this is not a problem for high-temperature applications, it will result in reduced aqueous corrosion resistance.
> ...In other words, you can expose grade 304 alloy steel to temperatures of up to 1,598 °F for short periods of time without ill effect, and for extended periods of time in temperatures of up to 1,697 °F. However, this can compromise the corrosion resistance of the metal, making it more susceptible to corrosion damage from exposure to moisture.”
That reduced aqueous corrosion resistance is problematic for our application, since we’re boiling water...And, since the flue gasses can reach 2000°F (or higher) in the localized center of the pot, that creates thermal stress issues as well. All of which would lead to accelerated rusting, wear, and then failure of the pot in the center of the bottom. This becomes even more of an issue considering the high
carbon content of flue gas, which has a “carburizing” corrosion effect on stainless steels.
The design I’m toying with currently uses Peter’s batch box Double ShoeBox Rocket design, and harvests the heat indirectly (after it has gone through some cooling by dispersion — by warming a mass of basalt pebble and sand, in which the pot sits, acting as a double-boiler of sorts...or like a “heating mantle” used in laboratory settings to bring Pyrex distillation boilers up to temp.)
If you’re working from a J-Tube design, I would recommend using the full barrel over the riser, and then placing your pot on the top of the barrel. This will allow the barrel to
bear the brunt of the heat dispersion, and will handle the carburizing effects of 2000°F flue gasses, instead of hitting your HLT directly with them. That barrel can be more cheaply and easily be replaced than a 304 stainless pot of that size...being more-or-less a sacrificial component of
rocket mass heater design.
Personally, I’m working from the doubleshoebox rocket design, because A) it lays the riser sideways and affords me more working vertical height than the traditional rocket, and B) loading a batch-box frees me up to do other brewing duties, whereas a J-tube must be constantly tended with fuel while it burns.
Cheers