[biofuels-biz] Re: hi ffa feed stocks

2002-08-28 Thread marcohgcardoso

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.


   
   
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[biofuels-biz] Re: hi ffa feed stocks

2002-08-27 Thread marcohgcardoso

Dear Michael,

I have plent of Palm Oil. When you mentioned that you used Straight 
Palm Oil you hadn't transerterificate the oil?

regards, Marco

--- 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.
  
  
 
 
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[biofuels-biz] Plant Information

2002-08-24 Thread marcohgcardoso

I have being reading many fantastic histories and sugestions here.
This, make me bring this question here and I hope anyone can help me.

I am looking for a basic plant to make around 10.000 liters month of 
BD.
I intend to use sunflower oil, soybean oil and other vegetable oil 
together with used vegetable oil from the food market.
Is there any company that offer a basic plant to process it?
I would like to use Ethanol instead of Methanol.
In the same time, is there any consultant or organization who provide 
information to help us to build this plant?

tks, Marco


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[biofuel] Re: process questions

2002-08-24 Thread marcohgcardoso

Dear Peter,

I am planning to do a batch with ethanol. Could you help me with it?

I am not sure about the process.

tks in advance,

Marco

--- In [EMAIL PROTECTED], Keith Addison [EMAIL PROTECTED] wrote:
 Hello Peter
 
 I have some questions regarding a 30 gallon batch I just made and
 would really appreciate some help.
 I have been using the 2 stage method this summer with success. I 
use
 6.25 grams of lye/litre of wvo with 25% of the volume of the wvo
 being methanol. 3/4 of that was added to the wvo and produced 
syrupy
 dark brown glycerine (like last time I made it). The next day I 
added
 the last 1/4 of the methoxide but did not get the gelatinous
 glycerine like I did last time, but got the dark liquidy syrup 
again.
 I am wondering why. Also, the final product is cloudy which might
 mean water in it. I have heated the final product to about 135-140
 for a half hour but it did not seem to permanently get rid of the
 cloudiness. I do not wish to do the wash at the end-I've been 
having
 success running unwashed, clear fuel.
 
 Are you sure? Have you done a respectable mileage and had the motor 
 examined? Washing makes the difference between having corrosive 
 contaminants in your fuel or not having them, no matter how nice it 
 might look.
 
 So, knowing that I should heat
 the wvo hotter and longer before the process
 
 What do you do with it before processing it?
 
 here are my questions:
 
 1) Why did I not get gelationous glycerine in the second stage?
 
 Only a couple of possibilities - either you didn't do the process 
in 
 the same way, or the oil was that much different.
 
 2 )Is the cloudiness water even though my reliable source of wvo 
does
 not let water get into his oil?
 
 How does he manage that? So you don't dewater the oil first? I 
don't 
 have too much faith in the idea of a reliable source. Not at all 
that 
 he's not a reliable man, but only an industry with a fully 
controlled 
 and standardized process will always produce just the same kind of 
 oil. Is he an industry? If he's a food outlet, does he produce the 
 same amounts and types of food every day, always prepared in the 
same 
 way?
 
 Anyway, to make sure that it is more or less regular, it might be 
an 
 idea to titrate a few batches so at least you know what you're 
 working with.
 
 Take a little of the cloudy biodiesel and put it in a blender with 
 about the same amount of water (same temperature as the biod), 
switch 
 on and see what happens. After a minute or two, switch off, and see 
 how long it takes to separate.
 
 3) What temp and how long do you need to heat the final product to
 evap the water-without evaporating the methanol (which boils off at
 140 degrees, I assume).
 
   The excess methanol will certainly evaporate before the water.
 
 4) Is the methanol that has successfully mixed with the oil in 
danger
 of boiling off above 140 degrees or will only the excess methanol
 boil off.
 
 Two fates of methanol - the stoichiometric quantity (depends on the 
 oil, say 12% v/v oil) becomes part of the methyl ester compound and 
 can't be evaporated short of evaporating the biodiesel itself, at a 
 much higher temp (it's a compound, not just a mixture). The excess 
 methanol, which functions to push the process towards completion, 
is 
 mostly left in the glycerine layer, with some still in the 
biodiesel. 
 You don't want it in your biodiesel, it's rather corrosive, one of 
 several good reasons to wash the fuel. This excess methanol will 
 evaporate on heating above 149F.
 
 5) If the cloudiness is water, why doesn't the water settle to the
 bottom the way it would after a wash? Why does it stay suspended?
 Does it eventually settle out to the bottom leaving clear bio-d on
 top?
 
 It might settle given time, but it's probably not water, it'll be 
 soaps or unconverted glycerides (process didn't go far enough) or 
 both. Either way, whether it settles or not, there'll still be 
traces 
 left in your fuel, and you should wash it.
 
 If you got lots of frothing with the sample in the blender, let it 
 settle for a week or two then give it a thorough bubble wash, then 
 let it settle again.
 
 Maintaining the temperature during the process is important. Mixing 
 times are averages - it depends on how big a batch you're doing, 
the 
 shape of your processor, speed of mixer, shape of the mixing blade. 
 If you're not getting near enough completion you could extend the 
 mixing time or increase the agitation. More likely it's other 
factors 
 at work, since your previous batch behaved differently and your 
 technique would have been the same or similar.
 
 Hope this helps. Please let us know how you fare.
 
 Best
 
 Keith
 
 
 My batch before this one came out crystal clear and the car purrs
 with it. I don't want to run a cloudy mix in the car, should I wait
 to see if it settles-or heat it up again? Again how hot, how 
long
 
 Thanks in advance,
 
 Peter
 
 
 
 
 
 
 
 Biofuel at Journey to Forever:
 

[biofuels-biz] Re: A processor question...

2002-08-19 Thread marcohgcardoso

 All,
 I would be glad if anyone could help me.

What is the porcentage of Ethanol and OHK that you are using to 
 transesterificate?
Do you use vegetal and solid fat too? What is the process diference?
 Do you do it in Batchs?
 How i the reaction temperature? How do you supply heat?
 Do you use to sell the gliceryn? How is the North American Market 
for 
 Glicerin.
 
 tks,
 Marco
 
 
 --- In [EMAIL PROTECTED], Keith Addison [EMAIL PROTECTED] wrote:
  Bill and all,
  
  Please excuse me if I offend anyone's sensibilities, but why
  would anyone pay $500 for a processor 1/3 the size of what they
  can create themselves for $50.00?
  
  Plus Heating Option: $100.
  
  There are bigger ones, 30, 40, 60, 80, 110 gallons ($850).
  
  Besides, having a reactor is one thing. What about the rest of
  the process? I kinda' doubt that these units take into
  consideration washing, waste water treatment, catalyst
  recover/neutralization, etc.
  
  All of that stuff is part of the process and should be
  included in the cost of a system.
  
  Sorry. There were no colorful pictures or spec sheets from which
  to gather a more informed opinion.
  
  If you go here:
  http://www.biodieselgear.com/equipment/index.htm
  
  ... and click on the [more info] buttons, there are pictures, but 
  only of the small unit, and it's not very clear - it talks about 
a 
  separate container for the meth but it's not pictured and it 
 doesn't 
  say if it's included. Washing is done in the processor using 
your 
  favorite wash method.
  
  Anyway, I agree - do it yourself. There are quite a few good 
 options 
  for that here:
  http://journeytoforever.org/biodiesel_processor.html
  
  Simon Wells' processor is a basic unit, very simple. Aleks Kac 
has 
 a 
  nice design there, Ian's vacuum biodiesel processor and Chuck 
 Ranum's 
  batch processor are both excellent set-ups.
  
  Okay, not everyone's into building stuff and salvaging, they may 
 not 
  have a workshop or the tools or the know-how. In that case I'd 
  suggest contacting Mike Pelly. His processor will be more 
expensive 
  than these Biodieselgear ones, but it's had some enthusiastic 
 reports 
  already, from experienced biodieselers. By all accounts Mike's 
done 
 a 
  really good job.
  Mike Pelly [EMAIL PROTECTED]
  
  On the other hand, if you want to wait a bit, not very long I 
 think, 
  there's a new design on the way for a basic 55-gallon drum 
 processor 
  you can easily assemble yourself, no welding, minimal tools, and 
 all 
  the parts, stirrers, motors, pumps, everything, will be sourced 
so 
  you can simply order them. This processor is designed to be 
cheap, 
  easy, effective and rugged, based on long experience of the 
 designer. 
  US-based.
  
  I'll announce that here and elsewhere when it's ready.
  
  Best
  
  Keith
  
  
  Todd Swearingen
  
  - Original Message -
  From: wmchellis [EMAIL PROTECTED]
  To: [EMAIL PROTECTED]
  Sent: Tuesday, August 13, 2002 12:50 AM
  Subject: [biofuels-biz] A processor question...
  
  
Hi all,
   
 Has anyone here tried the Biodieselgear.com processors?
If so, what can you tell me about them? Are they worth the
  money?
   
   
Thanks, -Bill Chellis


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[biofuels-biz] Re: A processor question...

2002-08-15 Thread marcohgcardoso

All,

I have some questuion inorder to compare my process with others.
What is the porcentage of Ethanol and OHK that you are using to 
transesterificate?
Do you do it in Batchs?
How i the reaction temperature? How do you supply heat?
Do you use to sell the gliceryn? How is the North American Market for 
Glicerin.

tks,
Marco


--- In [EMAIL PROTECTED], Keith Addison [EMAIL PROTECTED] wrote:
 Bill and all,
 
 Please excuse me if I offend anyone's sensibilities, but why
 would anyone pay $500 for a processor 1/3 the size of what they
 can create themselves for $50.00?
 
 Plus Heating Option: $100.
 
 There are bigger ones, 30, 40, 60, 80, 110 gallons ($850).
 
 Besides, having a reactor is one thing. What about the rest of
 the process? I kinda' doubt that these units take into
 consideration washing, waste water treatment, catalyst
 recover/neutralization, etc.
 
 All of that stuff is part of the process and should be
 included in the cost of a system.
 
 Sorry. There were no colorful pictures or spec sheets from which
 to gather a more informed opinion.
 
 If you go here:
 http://www.biodieselgear.com/equipment/index.htm
 
 ... and click on the [more info] buttons, there are pictures, but 
 only of the small unit, and it's not very clear - it talks about a 
 separate container for the meth but it's not pictured and it 
doesn't 
 say if it's included. Washing is done in the processor using your 
 favorite wash method.
 
 Anyway, I agree - do it yourself. There are quite a few good 
options 
 for that here:
 http://journeytoforever.org/biodiesel_processor.html
 
 Simon Wells' processor is a basic unit, very simple. Aleks Kac has 
a 
 nice design there, Ian's vacuum biodiesel processor and Chuck 
Ranum's 
 batch processor are both excellent set-ups.
 
 Okay, not everyone's into building stuff and salvaging, they may 
not 
 have a workshop or the tools or the know-how. In that case I'd 
 suggest contacting Mike Pelly. His processor will be more expensive 
 than these Biodieselgear ones, but it's had some enthusiastic 
reports 
 already, from experienced biodieselers. By all accounts Mike's done 
a 
 really good job.
 Mike Pelly [EMAIL PROTECTED]
 
 On the other hand, if you want to wait a bit, not very long I 
think, 
 there's a new design on the way for a basic 55-gallon drum 
processor 
 you can easily assemble yourself, no welding, minimal tools, and 
all 
 the parts, stirrers, motors, pumps, everything, will be sourced so 
 you can simply order them. This processor is designed to be cheap, 
 easy, effective and rugged, based on long experience of the 
designer. 
 US-based.
 
 I'll announce that here and elsewhere when it's ready.
 
 Best
 
 Keith
 
 
 Todd Swearingen
 
 - Original Message -
 From: wmchellis [EMAIL PROTECTED]
 To: [EMAIL PROTECTED]
 Sent: Tuesday, August 13, 2002 12:50 AM
 Subject: [biofuels-biz] A processor question...
 
 
   Hi all,
  
Has anyone here tried the Biodieselgear.com processors?
   If so, what can you tell me about them? Are they worth the
 money?
  
  
   Thanks, -Bill Chellis


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[biofuel] Equipment Information

2002-06-06 Thread marcohgcardoso

I am knew in thsi list.

I would like to produce sunflower oil and I don't know what kind of 
equipment i should use. Could you help me?

And, do you usually burn it with glicerin or take it out? What about 
motor problems after 200 hours for waste acumulation inside motor?

regards, 


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[biofuel] Equipment Information

2002-06-06 Thread marcohgcardoso

I am knew in thsi list.

I would like to produce sunflower oil and I don't know what kind of 
equipment i should use. Could you help me?

And, do you usually burn it with glicerin or take it out? What about 
motor problems after 200 hours for waste acumulation inside motor?

regards, 


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