Dear Marco,

I presume that you have read the
http://journeytoforever.org/biodiesel_svo.html and
their stuff on ethanol? It is an excellent place to
start and concisely sets out all the major
constraints.

Our work with agricultural engines showed that there
is a considerable difference between the injection
ports of small agricultural diesels so it might be a
bit dangerous to generalise.

Essentially though, we recommend starting and stopping
on petro-diesel (or biodiesel if available). The
exhaust pipe for the engine is taken out through a
simple one-pass heat exchanger in the palm-oil fuel
tank. After about 5 mins running on petro-diesel, the
40 litres of palm oil is warm enough to have similar
flow properties as petro-diesel. So we turn off one
fuel supply and move to the other.

We also recommend running the engine on petro-diesel
for the last five minutes of operation too. That way,
everything is left free of fatty-acid residues which
might cause corrosion (particularly if the engine is
not going to be used for a while.)

Ambient temperatures here rarely fall below 27C or
rise above 34C. As a consequence, SPO is always
liquid. This means that with some engines, you can
actually start them on palm-oil. But we don't
recommend it.  

Where are you precisely? What sort of engines do you
want to use SPO with? What operations do you want the
engines to perform (electricity generation, pumping,
transport, ploughing etc.). What are your ambient
temperatures?

I have some experience of using ethanol/methanol
blends with petroleum for spark-ignition engines. We
did this work in New Zealand about twenty years ago
and the results are well documented. However these are
highly volatile fuels with low-flash points and are
nothing like palm-oil really.

Regards

Michael


--- marcohgcardoso <[EMAIL PROTECTED]>
wrote:
> Dear Michael,
> 
> tks a lot for your help. So, we can use palm oil
> direct without 
> transes.?
> WHich motor modifications do you usually do?
> 
> Do you know how to do the sme process with Ethanol?
> Or anyone who 
> does it?
> 
> regards,
> 
> Marco
> 
> --- In [EMAIL PROTECTED], Michael Allen
> <[EMAIL PROTECTED]> wrote:
> > Dear Marco,
> > 
> > 
> > > I have plent of Palm Oil. When you mentioned
> that
> > > you used Straight 
> > > Palm Oil you hadn't transerterificate the oil?
> > 
> > That is correct. The first stage of our program
> was to
> > demonstrate that oil-palm growers could run their
> farm
> > machinery on straight palm oil (SPO)by making
> simple
> > engine modifications. The overall aim of the
> program
> > is to stabilise oil prices for oil-palm growers.
> That
> > means that we are looking at all aspects of
> palm-oil
> > use.
> > 
> > Incidentally, with respect to the high free fatty
> acid
> > feeds, the limit to the amount of FFA possible is 
> > probably related to the formation of water in
> Alek's
> > first stage esterification using sulfuric acid as
> the
> > catalyst. Thus 5%FFA in the oil means that 4mls of
> > water are produced for every litre of oil. This
> water
> > increases soap formation in the second stage
> (which is
> > catalysed by sodium hydroxide).
> > 
> > Alek Kak's method
> >
>
(http://journeytoforever.org/biodiesel_aleksnew.html)
> > reduces this impact by using 95% pure sulfuric
> acid
> > which has a strong affinity for water. He also
> > recommends about 9 times the amount of methanol
> > theoretically needed to react with the FFA. This
> also
> > has the effect of reducing the water
> concentration. 
> > 
> > So, for high(er) FFA, more methanol and more
> sulfuric
> > acid should be beneficial. However, that means
> more
> > sodium hydroxide to neutralise the acid and some
> form
> > of methanol recovery system. We use a simple
> condenser
> > connected to the reactor to grab the methanol. We
> can
> > either recycle this to the next batch or operate
> the
> > reactor under total reflux. This makes it possible
> to
> > operate the reactor at a higher temperature and so
> > accelerate the rate of the separate reactions.
> > 
> > Hope this gives you some useful ideas
> > 
> > Regards
> > 
> > Michael Allen
> > > 
> > > --- In [EMAIL PROTECTED], Michael Allen
> > > <[EMAIL PROTECTED]> wrote:
> > > > Dear David,
> > > > 
> > > > We did extensive work last year on heated
> Straight
> > > > Palm Oil (SPO) in two-wheeled tractors and
> fishing
> > > > boat motors. We had field trials by local
> farmers
> > > of
> > > > four commercial tractors and did test-bed work
> > > with
> > > > three others. Crude palm oil caused erosion of
> the
> > > > pistons by late ignition but refined palm-oil
> (of
> > > the
> > > > grade used for cooking oil) worked well. But
> we
> > > never
> > > > got around to using it in a locomotive.
> > > > 
> > > > This year we have been trying a range of
> reactor
> > > > designs to optimise methyl ester production
> from
> > > > refined oil. We are now moving back through
> > > various
> > > > forms of oil "refinement" towards the crude
> palm
> > > oil
> > > > (CPO). And yes, we are currently using the
> Aleks
> > > Kak
> > > > two-stage process. And yes it is currently at
> > > > atmospheric pressure (although the reactor was
> > > > designed to handle 200 kPa mainly as a safety
> > > feature.
> > > > Even so, some enthusiastic welders have
> > > > "overpressurised" it twice now through
> forgetting
> > > to
> > > > flood (and then drain) it with water before
> > > modifying
> > > > the unit).
> > > > 
> > > > The locomotive I mentioned is running on a B50
> > > blend:
> > > > It uses esters from a one stage
> > > trans-esterification
> > > > reaction of methanol with the stearin and
> palmitin
> > > > which has separated from the CPO. This waxy
> stuff
> > > is
> > > > probably quite comparable with the good
> Scottish
> > > lard.
> > > > 
> > > > Lots of luck!
> > > > 
> > > > Michael Allen
> > > > 
> > > > --- Keith Addison <[EMAIL PROTECTED]> wrote:
> > > > > >Thanks for your response, prof. Allen. 
> I'll
> > > > > formulate an inquiry to
> > > > > >Mohammed Farid as you suggest.  You
> mentioned
> > > Thai
> > > > > railway application. I
> > > > > >saw somewhere that German railways are
> using
> > > SVO in
> > > > > some of their shunting
> > > > > >engines.
> > > > > 
> > > > >
> > > >
> > >
> >
>
http://www.wired.com/news/technology/0,1282,53591,00.html
> > > > > Choo-Choo Trains on Energy Crunch
> > > > > 
> > > > > >The encouraging part of your message is you
> are
> > > > > reacting at 60C and that
> > > > > >this is near methanol boiling point.  That
> > > implies
> > > > > you are succeeding at
> > > > > >atmospheric pressure. Do you use conc.
> > > sulphuric
> > > > > acid first stage?  I agree
> > > > > >meth recovery is so simple that using
> excess is
> > > not
> > > > > really a problem.
> > > > > >
> > > > > >David T.
> > > > > 
> > > > > 
> > > > 
> > > > 
> > > >
> __________________________________________________
> > > > Do You Yahoo!?
> > > > Yahoo! Finance - Get real-time stock quotes
> > > > http://finance.yahoo.com
> > > 
> > > 
> > 
> > 
> 
=== message truncated ===


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