Keith -- I can see alcohol distillation as a by product of a boiler vapor
cycle.

But not at the present low temps. With butane as working fluid -- for
example -- it would be nice to be operating at 400 F.

Now -- here is the plan -- condense alcohol at higher temperature under
pressure!

Verbal flow diagram.

Think of a pressurized distillation column.

You could direct fire or steam heat the mash. Which would boil up through
the column. Condensers at the top -- with redirects for the effluents.

Water would return to the pot -- alcohol separated and out of this system.

I would have to look up the vapor characteristics of alcohol -- but just to
"guess"

Water would be condensing at 445 F at 400 psi pressure. Alcohol would not!

First stage is condensing the water out at 445 F -- second stage would be
condensing the alcohol out by further reducing its temperature -- higher up
the same column.

In both cases temperature reduction for condensation is accomplished by
boiling butane -- which in turn produces power using an Ormat style device.

You now have a power plant that distills alcohol as a side line! Greatly
reducing heat requirements/losses.

Further -- if you can get the vapor tables for alcohol -- you may find a
larger spread in condensing temperatures exist at these pressures -- which
would mean better extraction efficiencies.

Has anyone used pressurized stills yet?

Directly introducing high pressure/temperature steam to the mash pot would
accomplish this purpose -

A 400 psi -- 445 F boiler is a simple -- old fashioned -- fire tube boiler.
Cheap and easy to acquire.

In the sugar cane example -- these are more or less the style boilers they
have now -- burning bagasse.

So there you go -- the bagasse would then be supplying steam for power and
distillation -- but all in one pass.

Hey - this could really change the way people are looking at this process.

Peter

Biofuel at Journey to Forever:
http://journeytoforever.org/biofuel.html
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