Re: [biofuel] Re: Reclaiming the methanol

2001-05-31 Thread Keith Addison


> > Any experience using glycerin as a heating fuel?
>Afraid not but very interested in same. With winter begining and an aging
>slow combustion stove I,m looking for alternatives.
>Some interesting postings on this subject over last month or so.
> Regards , Paul

Be sure you have efficient combustion or you risk releasing toxins (acroleine).

Keith Addison
Journey to Forever
Handmade Projects
Tokyo
http://journeytoforever.org/

 


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-31 Thread Paul Gobert

- Original Message -
From: "Gary and Jos Kimlin" <[EMAIL PROTECTED]>
Subject: Re: [biofuel] Re: Reclaiming the methanol


> Paul my next batch will be with cotton seed oil. I intend to use the
> twostage with KOH rather than NaOH. The best I can do with NaOH seems to
be
> 80-85% pure,

Pure reagent grade NaOH can be obtained from chemical supply warehouses.
Various grades of purity (not water content) are available. Analytical grade
is not needed, technical grade is more than suitable.
suspect that leaves too much water to avoid soaps. I'll take
 >KOH is $100/25kg and Methanol $30/20l drum.
 Will check up on local prices and advise. Haven't had to buy methanol yet
 friend gave me 2 20L drums) but think that it is about $200.00 Australian
for a 200L drum.

> Any experience using glycerin as a heating fuel?
Afraid not but very interested in same. With winter begining and an aging
slow combustion stove I,m looking for alternatives.
Some interesting postings on this subject over last month or so.
 Regards , Paul


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-31 Thread Paul Gobert


- Original Message - >  Paul, one vessel would be great,
but poses (at first glance) two
> problems:
> -JIM

Points taken Jim,
Am trying to simplify process as much as possible. Even tried methylated
spirits for methoxide against all advice (40% water) and ended up with a
jelly like liquid resembling "pears" soap.
Simplification also involves the reduction of time to produce the BD as I
could be using this time for other productive work.
At this stage the plan goes something like this.

Feedstock: Used cottenseed oil supplied in 20L drums.
Conversion: Methoxide added to cold oil in drums, stirring for a few
minutes. Process 4 drums at a time.
Glycerol sets firm in bottom of drum after 24hr
standing allowing BD to be poured off.
Washing: S/H slow combustion H/W unit with inbuilt booster element.
Pump to circulate wash water from base of unit
delivering large drops of water over surface.
Drying: Water drained off after settling and during heating.
Filtering: System undecided.
Storage: directly into vehicle tank (130L) or jerry cans.

Still a few things to investigate
1) does cold processing produce a suitable product or is warm processing
better.
Esterification appears to be complete with cold process. Will compare the
products.
2). NaOH difficult to dissolve in methanol time/energy consuming.
Will try a batch using methoxide made by adding a concentrated aqueous
solution of NaOH to methanol.


Regards,
Paul




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RE: [biofuel] Re: Reclaiming the methanol

2001-05-29 Thread jerry dycus


Hi All,
For those who are reclaiming methanol what %
of the methanol do you get back? I assume vacuum
recovery method.
 Thanks, 
  jerry dycus 

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RE: [biofuel] Re: Reclaiming the methanol

2001-05-29 Thread kirk

$2 a pound for KOH? How much does KCl cost?

-Original Message-
From: Gary and Jos Kimlin [mailto:[EMAIL PROTECTED]
Sent: Monday, May 28, 2001 5:26 AM
To: biofuel@yahoogroups.com
Subject: Re: [biofuel] Re: Reclaiming the methanol


Paul my next batch will be with cotton seed oil. I intend to use the
twostage with KOH rather than NaOH. The best I can do with NaOH seems to be
80-85% pure, I suspect that leaves too much water to avoid soaps. I'll take
your advice and wash and dry it. I'll let you know how it goes. The oil
collectors here buy the oil and sell to a soap factory. I'll need more
experience to determine the break even point on oil cost, so far KOH is
$100/25kg and Methanol $30/20l drum. I need to calculate the average energy
cost. Any experience using glycerin as a heating fuel?


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-28 Thread Gary and Jos Kimlin

Paul my next batch will be with cotton seed oil. I intend to use the
twostage with KOH rather than NaOH. The best I can do with NaOH seems to be
80-85% pure, I suspect that leaves too much water to avoid soaps. I'll take
your advice and wash and dry it. I'll let you know how it goes. The oil
collectors here buy the oil and sell to a soap factory. I'll need more
experience to determine the break even point on oil cost, so far KOH is
$100/25kg and Methanol $30/20l drum. I need to calculate the average energy
cost. Any experience using glycerin as a heating fuel?


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-28 Thread zh24mij


 Paul, one vessel would be great, but poses (at first glance) two 
problems:
 Time and batch quantity, which is to say that you'd be producing a 
smaller batch over a longer period of time. Sure, it's compact, but for a 
garage operation I'd prefer a multi-barrel approach allowing many batches to 
be mixed, settled, washed and stored at the same time. 

Just a thought!

-JIM


[Non-text portions of this message have been removed]


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-27 Thread Paul Gobert


- Original Message -

> Treat anything clear as Methanol.
> My first attempt making biod, just sucking in Meth and at a temp of 55oC I
> found at least 250ml of Meth in my liquid trap.
> Be very careful.
> Ian

Ian,
In my trial laboratory scale batches have found that methoxide and SVO
(cottenseed in this case) do not mix readily. Would suggest that the
addition should be at a slow rate or stirring rate increased during the
addition.

Local fish and chip shop recently changed from solid veg oil (Frytol) to
cottenseed oil. About the same time the people collecting SVO decided to
charge for its removal. Owner is happy to give me the oil but I suspect that
he wants some biodiesel in return.

My initial trials were on refined safflower oil and various methods gave
good results.
Cottenseed oil has the advantage of being an oil at room temperature and can
easily be transfered to the reaction vessel.
To reduce variables the oil was first washed and then heated to 160 deg C
15% Methanol and 6.5g/litre NaOH  at 55 deg C produced a heavy gelatinous
deposit of glycerine/soap  which set solid after 24 hours. Would have to be
drained from the vessel much earlier or dug out the next day.
Reduction of the ammount of NaOH produced much less deposit. As low as 3g/L
( below that suggested as required for the reaction with acid free oil) gave
a managable product. Yet to compare the biodiesel from these batches( S.G.
and viscosity) to determine suitability of product.

"Foolproof two stage method" gave good results with this oi, probably
because of the smaller ammount of NaOH specified.  The product from the two
stage method however turned cloudy after a few weeks forming a whitish
suspension over time and seemingly reverting back to the heavier oil. This
batch had not been washed and I suspect that that could have been the
problem. Other batches washed and heat dried, have remained crystal clear.

Washing the product has presented problems. The cottenseed biodiesel and
reaction products/excess reagents mix tends to emulsify readily with water
forming a whitish flock.
Small scale washing using aquarium pump and stone was out of the question,
too much agitation and emulsion formation.  Most sucessful washing technique
so far involved gentle addition of large water droplets to surface of
biodiesel. Water collecting at bottom of wash vessel is pumped up to top and
sprinkled onto B/D.
Intend to use this system on production vessel. At this point am working
towards using the one vessel for reaction/washing/drying.

Will let you know how things go,
Regards Paul.





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[biofuel] Re: Reclaiming the methanol

2001-05-26 Thread scrof

Sorry, Mike, I didn't make it very clear, did I?  I've used much more 
than 30 gallons in processing fuel.  In total, I have recovered and 
reused about 30 gallons.

Dale

--- In [EMAIL PROTECTED], Mike Brownstone <[EMAIL PROTECTED]> wrote:
> Dale,
> 
> Isn't there any loss of methanol during reaction?  I am surprised 
that you
> are recovering all that you use.  Or did I mis-understand you?
> 
> Mike
> 



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[biofuel] Re: Reclaiming the methanol

2001-05-26 Thread scrof

I think you may be near the correct answer for a mixture only of 
water and methanol.  The boiling point of mixtures can be calculated, 
but are easier to find experimentally.  However, in recovering 
methanol from biodiesel byproduct we have a much more complex 
mixture.  Any water in the mix is either tied up in soap or, at the 
very least, heavy in dissolved catalyst.  Either will make the water 
much more difficult to boil.  I haven't taken my rig up to high 
enough temperature to after methanol recovery to recover any water, 
so I can't be sure at what temperature and pressure water recovery 
would begin, but suspect it would be at a very high temp or low 
pressure.

Dale


--- In [EMAIL PROTECTED], Keith Addison <[EMAIL PROTECTED]> wrote:
> > >
> 
> Hi Dale
> 
> Thanks, good info.
> 
> >I don't think water can be
> >recovered from the byproduct at anywhere near the boiling point of
> >methanol.
> 
> Now let's see if I can get this right. If it's a mixture of 
methanol 
> and water that's being boiled, the boiling point of the mixture 
will 
> be somewhere between the two boiling points, depending on the 
> proportion of the mix. Of course vapours come off before boiling 
> point is reached, but the methanol component won't boil off at the 
> boiling point of pure methanol (64.7 deg C), while the water 
> component remains unboiled until the temperature reaches 100 deg C. 
> If you evaporate a liquid mixture, the vapour has a higher 
proportion 
> of the more volatile components than the liquid it evaporated from. 
> Alcohol is more volatile than water (it takes less energy to 
vaporise 
> alcohol than to vaporise water). So when you boil a mix of the two, 
> the vapour contains more alcohol - not because the alcohol 
component 
> of the mix is boiling first, but because the alcohol is more 
> volatile. So the proportion of alcohol in the boiling liquid 
steadily 
> goes down, and the boiling point of the mixture steadily goes up. 
In 
> a 50-50 mix the boiling point will start off being halfway between 
> the boiling points of the two components - more alcohol lowers the 
> boiling point, more water raises it. If you boil a mix of methanol 
> and water, you'll get vapours of both.
> 
> (How did I do, O Silent One?)
> 
> If I screwed up, Dale, I'll no doubt be hearing about it and will 
> post a correction.
> 
> Thanks again.
> 
> Keith Addison
> Journey to Forever
> Handmade Projects
> Tokyo
> http://journeytoforever.org/


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-26 Thread ian

Treat anything clear as Methanol.
My first attempt making biod, just sucking in Meth and at a temp of 55oC I
found at least 250ml of Meth in my liquid trap.
Be very careful.
Ian
- Original Message -
From: Keith Addison <[EMAIL PROTECTED]>
To: 
Sent: Friday, May 25, 2001 7:59 AM
Subject: [biofuel] Re: Reclaiming the methanol


> >I've used and re-used about thirty gallons of methanol so far using
> >my hot pink vacuum still.  At first I was worried about recovering
> >water at the end of a run, so watched the condensate closely for any
> >sign of cloudiness. I've never seen any.  I don't think water can be
> >recovered from the byproduct at anywhere near the boiling point of
> >methanol.
> >
> >Dale
> >
> >--- In [EMAIL PROTECTED], Keith Addison <[EMAIL PROTECTED]> wrote:
> > > >Keith Addison asks:
> > > >
> > > > >A biodiesel question. If you boil off and distill the excess
> >methanol
> > > > >from the glycerine for re-use, is it in fact suitable for re-use?
> >
>
> Hi Dale
>
> Thanks, good info.
>
> >I don't think water can be
> >recovered from the byproduct at anywhere near the boiling point of
> >methanol.
>
> Now let's see if I can get this right. If it's a mixture of methanol
> and water that's being boiled, the boiling point of the mixture will
> be somewhere between the two boiling points, depending on the
> proportion of the mix. Of course vapours come off before boiling
> point is reached, but the methanol component won't boil off at the
> boiling point of pure methanol (64.7 deg C), while the water
> component remains unboiled until the temperature reaches 100 deg C.
> If you evaporate a liquid mixture, the vapour has a higher proportion
> of the more volatile components than the liquid it evaporated from.
> Alcohol is more volatile than water (it takes less energy to vaporise
> alcohol than to vaporise water). So when you boil a mix of the two,
> the vapour contains more alcohol - not because the alcohol component
> of the mix is boiling first, but because the alcohol is more
> volatile. So the proportion of alcohol in the boiling liquid steadily
> goes down, and the boiling point of the mixture steadily goes up. In
> a 50-50 mix the boiling point will start off being halfway between
> the boiling points of the two components - more alcohol lowers the
> boiling point, more water raises it. If you boil a mix of methanol
> and water, you'll get vapours of both.
>
> (How did I do, O Silent One?)
>
> If I screwed up, Dale, I'll no doubt be hearing about it and will
> post a correction.
>
> Thanks again.
>
> Keith Addison
> Journey to Forever
> Handmade Projects
> Tokyo
> http://journeytoforever.org/
>
>
>
>
> Biofuel at Journey to Forever:
> http://journeytoforever.org/biofuel.html
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>
>
>


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Re: [biofuel] Re: Reclaiming the methanol

2001-05-25 Thread David Teal

Dale is right, recovered methanol is OK to re-use.  I have found that from
biod made using 15% meth (v/v WVO), the glyc. yields 3% meth (v/v WVO) and
is well worth the trouble of simple distillation at 70 deg C.  Probably will
use 20% in future for an easier life without unnecessary loss of costly
reagent.

David T


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RE: [biofuel] Re: Reclaiming the methanol

2001-05-25 Thread Mike Brownstone

Dale,

Isn't there any loss of methanol during reaction?  I am surprised that you
are recovering all that you use.  Or did I mis-understand you?

Mike

-Original Message-
From: [EMAIL PROTECTED] [mailto:[EMAIL PROTECTED]
Sent: Friday, May 25, 2001 3:29 AM
To: biofuel@yahoogroups.com
Subject: [biofuel] Re: Reclaiming the methanol


I've used and re-used about thirty gallons of methanol so far using
my hot pink vacuum still.  At first I was worried about recovering
water at the end of a run, so watched the condensate closely for any
sign of cloudiness. I've never seen any.  I don't think water can be
recovered from the byproduct at anywhere near the boiling point of
methanol.

Dale

--- In [EMAIL PROTECTED], Keith Addison <[EMAIL PROTECTED]> wrote:
> >Keith Addison asks:
> >
> > >A biodiesel question. If you boil off and distill the excess
methanol
> > >from the glycerine for re-use, is it in fact suitable for re-use?



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[biofuel] Re: Reclaiming the methanol

2001-05-25 Thread Keith Addison

>I've used and re-used about thirty gallons of methanol so far using
>my hot pink vacuum still.  At first I was worried about recovering
>water at the end of a run, so watched the condensate closely for any
>sign of cloudiness. I've never seen any.  I don't think water can be
>recovered from the byproduct at anywhere near the boiling point of
>methanol.
>
>Dale
>
>--- In [EMAIL PROTECTED], Keith Addison <[EMAIL PROTECTED]> wrote:
> > >Keith Addison asks:
> > >
> > > >A biodiesel question. If you boil off and distill the excess
>methanol
> > > >from the glycerine for re-use, is it in fact suitable for re-use?
>

Hi Dale

Thanks, good info.

>I don't think water can be
>recovered from the byproduct at anywhere near the boiling point of
>methanol.

Now let's see if I can get this right. If it's a mixture of methanol 
and water that's being boiled, the boiling point of the mixture will 
be somewhere between the two boiling points, depending on the 
proportion of the mix. Of course vapours come off before boiling 
point is reached, but the methanol component won't boil off at the 
boiling point of pure methanol (64.7 deg C), while the water 
component remains unboiled until the temperature reaches 100 deg C. 
If you evaporate a liquid mixture, the vapour has a higher proportion 
of the more volatile components than the liquid it evaporated from. 
Alcohol is more volatile than water (it takes less energy to vaporise 
alcohol than to vaporise water). So when you boil a mix of the two, 
the vapour contains more alcohol - not because the alcohol component 
of the mix is boiling first, but because the alcohol is more 
volatile. So the proportion of alcohol in the boiling liquid steadily 
goes down, and the boiling point of the mixture steadily goes up. In 
a 50-50 mix the boiling point will start off being halfway between 
the boiling points of the two components - more alcohol lowers the 
boiling point, more water raises it. If you boil a mix of methanol 
and water, you'll get vapours of both.

(How did I do, O Silent One?)

If I screwed up, Dale, I'll no doubt be hearing about it and will 
post a correction.

Thanks again.

Keith Addison
Journey to Forever
Handmade Projects
Tokyo
http://journeytoforever.org/

 


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[biofuel] Re: Reclaiming the methanol

2001-05-25 Thread scrof

I've used and re-used about thirty gallons of methanol so far using 
my hot pink vacuum still.  At first I was worried about recovering 
water at the end of a run, so watched the condensate closely for any 
sign of cloudiness. I've never seen any.  I don't think water can be 
recovered from the byproduct at anywhere near the boiling point of 
methanol.

Dale 

--- In [EMAIL PROTECTED], Keith Addison <[EMAIL PROTECTED]> wrote:
> >Keith Addison asks:
> >
> > >A biodiesel question. If you boil off and distill the excess 
methanol
> > >from the glycerine for re-use, is it in fact suitable for re-use?



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