If using the Acid process you will generate some water. Also remember 
the oil is dry but there are trace amounts of water in the best grease 
but I dont think this causes a problem.
JIM

Jonathan Schearer wrote:

> I am probably missing something, but where would the water be coming 
> from in the first place?  Isn't the waste oil you start with not 
> supposed to contain any water, and if it does, you need to boil it 
> off?  Then there's the methanol.  It should not contain any water 
> either.  I don't believe the catalyst would contain any water either.  
> It is the waste glycerin layer that contains most of the methanol, 
> correct?  I have been told that the only stupid question is the one 
> that isn't asked.  So I'm asking...where is the water coming from?
>
> */Michael Gian <[EMAIL PROTECTED]>/* wrote:
>
>
>     In additon, a fractionating column requires a reflux, the partial
>     return and
>     recycling of distillate product from the condenser back down the
>     fractionating
>     column which increases the energy tax (energy costs) of purifying the
>     methanol.
>
>     This is true for tray towers. A more elegant setup is a packed
>     fractionating column, aka reflux column. Years ago we made one
>     packed with
>     small glass beads for jewelry, picked up cheap at a garage sale.
>     Ethanol
>     production, in this case not intended to fuel machinery. What
>     works for
>     ethanol will work for methanol, probably better, given no water
>     azeotrope.
>
>     Alcohol Fuel Manual Ch11 has the poop.
>
>     Michael Gian
>
>     Mike McGinness
>
>     bob allen wrote:
>
>     > without getting into excessive detail, the boiling point of a
>     mixture is
>     > the weighted average of the stuff present. At first you have pure
>     > methanol coming off. as the temperature rose, increasing amounts of
>     > water contaminated the alcohol.
>     >
>     > You need a fractionating column to obtain pure methanol.
>     >
>     > Joe Street wrote:
>     > > 3A sieves will work but are normally used for getting tiny
>     amounts of
>     > > water out of solvents to bring them into the low ppm range.
>     They will
>     > > work of course but you might saturate them and have to do a second
>     > > stage. There is a significant energy input into regenerating
>     the seives
>     > > as well. You have to bake them at well over 100 degrees C more
>     like
>     > > 200, but you can get by with lower temps if you bake them out with
>     > > vacuum. Try putting a thermometer in your condenser and
>     monitor vapour
>     > > temperature to get a better endpoint and you will have an
>     easier time.
>     > > You have answered some of my own questions. I have recovered some
>     > > methanol but not tried to use it yet. Sounds like if straight
>     > > distillation is carefully done the methanol is dry enough to
>     use without
>     > > further drying. Great news and thanks for the post! :)
>     > >
>     > > I have some excellent references on solvent drying I can mail
>     you if you
>     > > want. No soft copy sorry but I might be able to scan them.
>     > >
>     > > Joe
>     > >
>     > > Thomas Kelly wrote:
>     > >> Good day to all,
>     > >> After splitting the glycerine coproduct from roughly 1200L of
>     > >> processed WVO, I distilled approximately 100L of the
>     > >> glycerine/methanol component.
>     > >> The first drops of methanol began to fall from the condenser at
>     > >> 145F. As the temp rose to 150F there was a steady flow of
>     clear liquid
>     > >> from the condenser. Throughout the day I turned the heat off
>     when the
>     > >> flow was steady and back on when it slowed.
>     > >> I filled a 4.5 gal (17.7L) cubie with clear liquid and started a
>     > >> second one. At this point the temp was over 160F. I let the
>     still run
>     > >> up to 200F. At this point the second cubie had 4 gallons of clear
>     > >> liquid (and it was now 1AM) giving a total of 8.5 gal. I was
>     thrilled
>     > >> with the result (and tired). I used the first 4.5 gal (17.7L)
>     to run
>     > >> one batch, and while that was settling ran a second batch
>     using the
>     > >> second 4 gal of recovered methanol.
>     > >> The first batch washed OK, but was a little slow to separate. It
>     > >> failed the methanol quality test.
>     > >> The second batch did not even pass the wash test.
>     > >> I have been making consistenly high quality BD for several
>     months ...
>     > >> thank you JtF and list members. I don't think I made mistakes in
>     > >> measurement or titration.
>     > >> My question:
>     > >> As my distillation temps rose towards 200F (93C) could I have
>     been
>     > >> including water in my distillate? (The methanol recovered at
>     lower
>     > >> temps performed better than the methanol recovered at higher
>     temps.)
>     > >> If so, can I use Zeolite "molecular sieves" in the future to
>     remove it?
>     > >>
>     > >> Thanks,
>     > >> Tom
>     >
>     >>
>     ------------------------------------------------------------------------
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