[biofuels-biz] switchgrass to electricity (PR)

2003-05-29 Thread murdoch

http://biz.yahoo.com/prnews/030529/atth008_1.html
 

Press Release Source: Southern Company 


Southern Company Testing Grass Cubes to Make Electricity
Thursday May 29, 10:01 am ET 


ATLANTA, May 29 /PRNewswire-FirstCall/ -- Southern Company today
announced that it is now using switchgrass and other local grasses
formed into small cubes to generate electricity. The grass cubes are
being mixed with coal at Southern Company's Plant Mitchell, near
Albany, Ga. Mitchell is owned and operated by the company's Georgia
Power subsidiary.
(LOGO: http://www.newscom.com/cgi-bin/prnh/20020207/SOCOLOGO )
Switchgrass is a native prairie grass grown easily in the South, and
when blended with coal as a fuel can reduce power plant emissions.
Initial testing of switchgrass was conducted at Southern Company's
Alabama Power Gadsden Steam Plant in the spring of 2001. Results
showed switchgrass not only to be a potential energy source but also
emissions of carbon dioxide, sulfur dioxide and mercury were reduced.

Based on the successful results achieved earlier from the switchgrass
co- firing at Plant Gadsden, Southern Company has committed to a
three-year demonstration of biomass co-firing at that plant, located
in Gadsden, Ala. Switchgrass, along with other biomass fuels, will be
tested in order to improve on initial test results, as well as to gain
more knowledge of biomass co-firing.

We've seen favorable results testing switchgrass as a potential
energy source, said Dr. Charles Goodman, Southern Company senior vice
president of research and environmental affairs. As Southern Company
diversifies its fuel portfolio to meet future energy demands, biomass,
such as switchgrass, is just one of several options we are currently
testing that may be beneficial in a low-cost, environmental-friendly
way.

The testing at Plant Mitchell uses two kinds of pelletized grass;
coastal Bermuda grass from Sunbelt Ag Expo in Moultrie, Ga., and
switchgrass from Alabama that was grown on 300 acres of farmland near
Lincoln and Winterboro. If used as an energy crop, switchgrass could
provide farmers with maximum yields and returns at minimal costs.

Plant Mitchell received 170 tons of the switchgrass cubes to be
pulverized and blended with varying amounts of coal to determine the
most efficient mixture. Southern Company is hoping that the compressed
switchgrass co-firing at Plant Mitchell can be done without having to
inject the grass separately as required in the initial testing at
Plant Gadsden.

Last year, Plant Gadsden's switchgrass pilot project won environmental
awards from the Electric Power Research Institute and the Southeastern
Electric Exchange.

With 4 million customers and nearly 37,000 megawatts of generating
capacity, Atlanta-based Southern Company (NYSE: SO - News) is the
premier super- regional energy company in the Southeast and a leading
U.S. producer of electricity. Southern Company owns electric utilities
in four states, a growing competitive generation company, an energy
services business and a competitive retail natural gas business, as
well as fiber optics and wireless communications. Southern Company
brands are known for excellent customer service, high reliability and
retail electric prices that are 15 percent below the national average.
Southern Company has been named two consecutive years No. 1 on Fortune
magazine's America's Most Admired Companies list in the Electric and
Gas Utility industry. Southern Company has more than 500,000
shareholders, making its common stock one of the most widely held in
the United States. Visit the Southern Company Web site at
www.southerncompany.com . 





Source: Southern Company 


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Re: [biofuels-biz] switchgrass to electricity (PR)

2003-05-29 Thread David Teal

Until the numbers get bigger, this possibly qualifuies as greenwash?  Good
idea in principle, though not exactly new.


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Re: [biofuel] blender batch

2003-05-29 Thread Clifford Ryer

Dan:

   I also did a first test batch of 3 liters wvo, adding 600ml methanol and 
got only 350ml of glycerine.  I didn't really know what to expect, but 10% 
relative to the original stock seemed kind of low to me as well.  Where did 
you get the notion (expectation) that you should get at least 200ml (20% of 
feedstock)?  I think both Dan and I would appreciate feed back on what 
kinds of glycerine vs biodiesel yields we should expect.  I have not come 
across much about this on any of the web-based material out there.  Does 
yield vary greatly with oil type and condition? When you have never done 
this before, its kind of difficult to interpret your results.

Cliff

At 08:31 AM 5/28/2003 -0700, you wrote:
Hi,

I did a blender test batch of biodiesel last night.  I
titrated to 2ml, so I used 5.5g of lye and mixed it in
with 200ml of methanol.  I then heated the oil up(1
litre), and put it in the blender, and mixed for 15-20
minutes.  It quickly began to separate and the
biodiesel at the very top inch of the blender after
the first 15 minutes or so was quite clear.  I woke up
in the morning and only 125 ml or glycerin settled out
and the biodiesel is cloudy.  It dropped to only 50
degrees last night.  Shouldn't there by at least 200
ml of glycerin settled at the bottom?  There are only
2 layers, the top, light and slightly cloudy, and the
dark glycerin.  Where is the extra 75 ml of glycerin,
and at what temp does the biodiesel clear up?  Thanks,

Dan
 


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Re: [biofuel] etanol + metanol

2003-05-29 Thread arie aw wiryawan

hai keith
thanks fo reply my email
i have already seen website you gave me, that;'s my reason why i interested to 
try it.what do you think?do you have any suggestion?
thanks



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Re: [biofuel] Two-stage Process - jelly?

2003-05-29 Thread Keith Addison

Hello Paul, Mark

See below...

- Original Message -
From: mark schofield [EMAIL PROTECTED]

  Hi
 
  So after playing with the single stage for a
  while, I have produced a good clear final
  product. I have bought a hot plate magnetic
  stirrer for $360 USD that has helped for
  titrations etc.
 
  I have played with the two stage process and the
  final product has turned to jelly. I have
  followed the 2-stage instructions exactly -
  timer, burettes, +/- 1mg weighing scale, 97%
  H2SO4, hot plate stirrer with closed loop
  temperature control and digit speed and temp
  output. The chemicals are all analytical grade
  and the oil requires only 0.1cc of 0.1M NaOH
  solution to pH 8.5.
 
  I heat 1000cc of oil up to 35'C. I add 80cc of
  99.5% Methanol and stir for 5 minutes. I then add
  1cc of 97% H2SO4 and stir for 1 hour. I then cut
  the heat and stir for a further hour. The mixture
  does not separate but is left for minimum 8hrs
  usually 12. I re-heat the still liquid mixture to
  55'C and add 3.5g NaOH and 120cc Methanol. I stir
  for 1 hr and leave to settle. The final product
  doesn't settle and congeals over time.
 
  Keith - I am lost. Some where along the line soap
  is formed. I will re-run the experiment and
  comment tomorrow.
 
  On a larger scale - could a 1um filter /
  coalescer unit be used to pre-process heated oil?
 
  Regards
 
  Mark

Hello Mark,
With oil of 0.1ml 0.1M (0.4%) NaOH titration use of the two stage acid base
method is not waranted. The aim of the acid stage is to esterify any FFA
present. From your titration we can see that the oil has very little FFA in
it to start with. It would be a better candidate for single base method.
Very little would be happening in the acid stage, there is almost no FFA to
esterify and acid catalysed transesterification is very slow. In this case
all that is happening is that you are acidifying (with sulphuric acid) the
oil/methanol mix prior to performing a base catalysed transesterification
and not taking that acidity into account when choosing the ammount of NaOH
to use.
When you rerun the experiment try using a larger quatity of NaOH in the
second stage. If you don't drain off the small ammount of acid/aqueous layer
after the first stage some of  the NaOH will be consumed neutralising it.
Also current thinking is that more than 3.5g/l gives a better conversion.
Both good reasons for using more than 3.5g/l in the second stage.

Would suggest using this oil for single base method and finding some oil
higher in FFA to trial the acid/base method.

Regards   Paul Gobert.

Paul, if this is the case then how/why does it work so well with 
virgin oil? Which it does. Also, why have so many people (more and 
more, despite a concerted disinformation campaign) now use it as 
their standard process, regardless of what kind of oil they use? - as 
Aleks recommended in the first place.

Mark, why not try it with virgin oil first? That's the common (and 
sound) advice when starting out with the single-stage process, and it 
applies equally well to any new process you're trying. Then you have 
some kind of benchmark to work from. Follow the instructions exactly 
so you start off with nice variable-free results, one way or the 
other. Use a standard sort of oil - canola, soy, sunflower, corn. If 
it doesn't work with virgin oil, then you're getting something wrong 
- maybe losing too much methanol vapour, as Girl Mark suggested. If 
it does work with virgin oil, but not with the WVO, then that narrows 
down your possible causes - perhaps there's water in the oil, or 
somewhere in the process.

Also current thinking is that more than 3.5g/l gives a better conversion.
Both good reasons for using more than 3.5g/l in the second stage.

Some current thinking is saying that, yes - sweeping statements 
across the board that no matter what, regardless of anything else, 
just use 5gm/litre. Fairly typical. And, no, not too impressed that 
GCs are said to be involved in proving it: say the magic words GC 
and nobody thinks any further. It all depends, as always. The 
following is a bit more sensible, IMO:

How much lye to use?
http://journeytoforever.org/biodiesel_make2.html#lyeamount

It requires 3.5 gm of NaOH lye per liter of oil as catalyst to 
transesterify new oil (virgin, uncooked).

Used oil (WVO) needs more lye than new oil, to neutralize the Free 
Fatty Acids (FFAs) formed in cooking the oil, which can slow or stop 
the transesterification process.

You have to titrate the oil to determine the FFA content and how much 
lye will be required. Titration measures the pH of the oil, ie the 
acid-alkaline level (pH7 is neutral, lower values are increasingly 
acidic, higher than 7 is alkaline, or base). From this you can 
calculate how much extra alkali (lye) will be needed to neutralize 
the FFAs.

The extra lye converts the FFAs to soap, which drops out with the 
glycerine layer.

Too much lye will make extra soap, very alkaline biodiesel that's 

Re: [biofuel] acid stage question

2003-05-29 Thread Keith Addison

Hello to all.

Question: If wvo is dried by boiling off water, can the acid stage be
undertaken once oil temp. falls below boiling point of methanol? Does higher
temp. affect esterification in any positive or negative way?

Bill C.

Hello Bill

Should be no problem. It's quite adaptable, but it's recommended that 
you get familiar with the standardized process first, according to 
Aleks's instructions. Then you have a solid baseline to work from in 
adapting it. One step at a time.

I said this in an earlier message:

One point on energy use in comparing the two main dewatering methods 
is that heating to 60-70 deg C and settling loses the heat, whereas 
with boiling it off, while using lots of energy, you can at least 
catch it on the way down and start processing the oil once it's 
cooled to 55 deg C, saving some of the extra energy. But more heat 
carries the danger of creating more FFAs, which adds to boiling being 
the less preferred method.

It depends on the oil - will you always be working with the same oil? 
Three possibilities: nice oil, no need for dewatering; heat to 60¡C 
and settle for 24 hours, draw from the top; boil the water off. We do 
all three of those at various times. From another previous message:

It seems heating to 60¡C and settling to separate water either works 
or it doesn't. Some people swear by it, others have no success. It 
may be due to the presence of animal fats in heavily used oils, which 
can be very difficult to remove the water content from. We've had 
mixed results. With oil from a new source we heat a sample to 100¡C 
to dewater (if any) and then process, then try the same with 60¡C and 
settling. (Or not if boiling shows there wasn't any water.)

Best wishes

Keith


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Re: [biofuel] etanol + metanol

2003-05-29 Thread Keith Addison

Hi Arie

hai keith
thanks fo reply my email

You're welcome!

i have already seen website you gave me, that;'s my reason why i 
interested to try it.what do you think?do you have any suggestion?

Go ahead and try it. Tell us what happens. Whatever happens, you'll 
get useful results for your project, no? There are people here who'll 
help you, I'm sure. But such general questions are difficult. Start 
your work, give us some more detail, then you'll get better responses.

Where are you, by the way?

Regards

Keith



thanks


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Re: [biofuel] Two-stage Process - jelly?

2003-05-29 Thread mark schofield

Dear Keith and All

Unlike some other e-mails I'll descibe exactly
what I have done.

500cc virgin vegetable oil (non-specific type)
Heated to 35'C
80cc 99.5% Methanol added
Stirred for 5 minutes
Add 0.5cc (10 drops) of 97% H2SO4
Stir at 35'C for 1 hour - 600 rpm
Stir without heat for 1 hr - 600 rpm
Settle for 8 hrs
[ At all time the vessel has been covered with
tightly fitting cling film with only a very small
hole for the thermo-couple to go in (maybe 1.5 to
2mm diameter). Methanol loss is negligable. ]

No glycerine at all. The product has not settled
but is still liquid. This is virgin oil never
used fresh from the super market ASDA here, now
owned by WoolMart.

This morning - heated the oil to 55'C. Will add
3.1g NaOH plus 120cc of Methanol. If this turns
to jelly then I will repeat again and see what
happens.

The single stage process works a treat every
time, producing good clean ME. 

Keith, so the extra NaOH on top of that required
to drive the reaction neutralises the FFA's (in
used oil) and extracts them as soap in the final
wash?

Regards

Mark :-(


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[biofuel] Diesel Boats

2003-05-29 Thread Jack Kenworthy

I have a question for any mechanic-types out there - particularly marine-diesel 
familiars.  I am thinking about purchasing a 40 foot diesel work boat for a 
combined aquculture and dive operation and I am wondering if any knows about:
1 - this engine in particular:  General Motors 8V71 twin turbo rated at 450 HP? 
 I know that GM has had some trouble with diesel engines in the past just 
wondering if anyone has experience or knowledge pertaining to this model in 
particular.
2 - Special considerations for using biodiesel in marine applications?
Thanks for the help.
Best,
Jack
Jack Kenworthy
Sustainable Systems Director
The Cape Eleuthera Island School
242-359-7625 ph. 954-252-2224 fax
www.islandschool.org

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[biofuel] switchgrass to electricity (PR)

2003-05-29 Thread murdoch

http://biz.yahoo.com/prnews/030529/atth008_1.html
 

Press Release Source: Southern Company 


Southern Company Testing Grass Cubes to Make Electricity
Thursday May 29, 10:01 am ET 


ATLANTA, May 29 /PRNewswire-FirstCall/ -- Southern Company today
announced that it is now using switchgrass and other local grasses
formed into small cubes to generate electricity. The grass cubes are
being mixed with coal at Southern Company's Plant Mitchell, near
Albany, Ga. Mitchell is owned and operated by the company's Georgia
Power subsidiary.
(LOGO: http://www.newscom.com/cgi-bin/prnh/20020207/SOCOLOGO )
Switchgrass is a native prairie grass grown easily in the South, and
when blended with coal as a fuel can reduce power plant emissions.
Initial testing of switchgrass was conducted at Southern Company's
Alabama Power Gadsden Steam Plant in the spring of 2001. Results
showed switchgrass not only to be a potential energy source but also
emissions of carbon dioxide, sulfur dioxide and mercury were reduced.

Based on the successful results achieved earlier from the switchgrass
co- firing at Plant Gadsden, Southern Company has committed to a
three-year demonstration of biomass co-firing at that plant, located
in Gadsden, Ala. Switchgrass, along with other biomass fuels, will be
tested in order to improve on initial test results, as well as to gain
more knowledge of biomass co-firing.

We've seen favorable results testing switchgrass as a potential
energy source, said Dr. Charles Goodman, Southern Company senior vice
president of research and environmental affairs. As Southern Company
diversifies its fuel portfolio to meet future energy demands, biomass,
such as switchgrass, is just one of several options we are currently
testing that may be beneficial in a low-cost, environmental-friendly
way.

The testing at Plant Mitchell uses two kinds of pelletized grass;
coastal Bermuda grass from Sunbelt Ag Expo in Moultrie, Ga., and
switchgrass from Alabama that was grown on 300 acres of farmland near
Lincoln and Winterboro. If used as an energy crop, switchgrass could
provide farmers with maximum yields and returns at minimal costs.

Plant Mitchell received 170 tons of the switchgrass cubes to be
pulverized and blended with varying amounts of coal to determine the
most efficient mixture. Southern Company is hoping that the compressed
switchgrass co-firing at Plant Mitchell can be done without having to
inject the grass separately as required in the initial testing at
Plant Gadsden.

Last year, Plant Gadsden's switchgrass pilot project won environmental
awards from the Electric Power Research Institute and the Southeastern
Electric Exchange.

With 4 million customers and nearly 37,000 megawatts of generating
capacity, Atlanta-based Southern Company (NYSE: SO - News) is the
premier super- regional energy company in the Southeast and a leading
U.S. producer of electricity. Southern Company owns electric utilities
in four states, a growing competitive generation company, an energy
services business and a competitive retail natural gas business, as
well as fiber optics and wireless communications. Southern Company
brands are known for excellent customer service, high reliability and
retail electric prices that are 15 percent below the national average.
Southern Company has been named two consecutive years No. 1 on Fortune
magazine's America's Most Admired Companies list in the Electric and
Gas Utility industry. Southern Company has more than 500,000
shareholders, making its common stock one of the most widely held in
the United States. Visit the Southern Company Web site at
www.southerncompany.com . 





Source: Southern Company 


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[biofuel] OT: ad hoc comment on Astropower situation

2003-05-29 Thread murdoch

Over the last few months Astropower stock has collapsed.  Although I
have allowed my indexes to be neglected, it is worth noting that at
one time it was clearly the obvious quality amongst many alternative
energy stocks of dubious quality, and it was a part of the
capitalization of my ae index.  

It had revenues, consistent revenue growth, profits, consistent profit
growth, etc.  They made product, they were among the world's top 15
producers, with many oil company subsidiaries and large company
subsidiaries competing against them, and they weren't going away.

Now they have gone away, from a stock market perspective.  Their CFO
and CEO, who was respected by others, have resigned in disgrace.  Well
intended green-mutual-funds who invested in them have been damaged.  

More than one source seems to indicate that the many hundreds of lower
workers throughout the company are not to blame, that they could
continue to do their thing and make solar product going forward.  But
what the heck has top management been doing to turn profits into
losses, retroactively?  Who the hell knows.  I think it's fair to
entertain the hypothesis that, quite simply, it is a case of fraud,
until there's some clarification.  The company, over many months, has
not bothered to clarify a goddamn thing.

What I want to say is that, in a way, this is only too logical.  A
couple of years ago I tried to sit down and make a list of enough
publicly traded nearly-pure-play PV companies so that I could make a
solar index, but it just didn't work out.  APWR was in the list of
course, and there were a few other sort-of plays, such as SPIR, ENER,
SWVG.F or something.

Anyway, I have been thinking that some of the criticism of the Bush
administration is shallow, and that a primary weapon of their is the
neglect of discussion of important topics, and the neglect of the
importance of ordering massive quantities of alternative energy
products, rather than paying lip service to alternative energies,
funding some research with a pittance, and then continuing the massive
river of money to traditional energy technologies.  

I see the collapse of one of the only decent non-oil-company-owned
alternative energy companies as something that the fossil fuel
lobbyists and others probably find hysterical.  Doubtless they will
sit around and smirk as to the corruption of those environmentalist
jokers.

One of APWRE's competitors, ENER (a subsidiary of theirs is United
Solar, although that's only a percentage of ENER) is now part-owned by
Chevron Texaco and I think has three or four decades of history of
slow growth which has benefited the founder and hurt long-term
investors irreparably.  Somehow they've always stayed afloat, perhaps
due to those government contracts which always seem to come in.  We
wouldn't want to perpetuate the idea that private sector demand could
keep a PV company in business.

So, APWRE is now in disgrace from a stock-market point of view, SPIR's
solar subsidiary plods along (recent quarter was at a loss), SWVG is
sort of a joke as far as I can see, stock-price-wise, etc. I doubt
Chevron-TExaco, Royal Dutch Shell, etc. are crying in their milk.
Doubtless they will try to make the case that it helps vindicate the
idea that the market for PV is not strong enough to stand on its own.
They will probably leave out that they helped, in my view, arrange for
that condition.

I haven't seen much mention or discussion of all this, so I am
mentioning it.

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Re: [biofuel] Diesel Boats

2003-05-29 Thread Neoteric Biofuels Inc

Common, reliable, used in all sorts of marine applications, buses, etc.

Known as Screaming Green Leakers I believe, for their noteworthy  
tendency to run and run, but leak lube oil from various places.

Just keep a rag handy.

Pretty heavy on fuel use...my 40' tug had a Perkins 354-6, under 100HP,  
yet could tow a small barge well, and was very economical. Do you  
really need all that horsepower??

Edward Beggs
http://www.biofuels.ca


On Thursday, May 29, 2003, at 06:09 AM, Jack Kenworthy wrote:

 I have a question for any mechanic-types out there - particularly  
 marine-diesel familiars.  I am thinking about purchasing a 40 foot  
 diesel work boat for a combined aquculture and dive operation and I am  
 wondering if any knows about:
 1 - this engine in particular:  General Motors 8V71 twin turbo rated  
 at 450 HP?  I know that GM has had some trouble with diesel engines in  
 the past just wondering if anyone has experience or knowledge  
 pertaining to this model in particular.
 2 - Special considerations for using biodiesel in marine applications?
 Thanks for the help.
 Best,
 Jack
 Jack Kenworthy
 Sustainable Systems Director
 The Cape Eleuthera Island School
 242-359-7625 ph. 954-252-2224 fax
 www.islandschool.org

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


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Re: [biofuel] acid stage question

2003-05-29 Thread William Clark

Thanks Keith,

I got 35 deg. C and 55 deg. C mixed up. Your earlier post makes more sense
to me now. Another question is, would raising the pressure in the processor
also raise the temp. at which I could begin stage one processing?

Thanks for your help.

Bill C.
- Original Message -
From: Keith Addison [EMAIL PROTECTED]
To: biofuel@yahoogroups.com
Sent: Thursday, May 29, 2003 3:20 AM
Subject: Re: [biofuel] acid stage question


 Hello to all.
 
 Question: If wvo is dried by boiling off water, can the acid stage be
 undertaken once oil temp. falls below boiling point of methanol? Does
higher
 temp. affect esterification in any positive or negative way?
 
 Bill C.

 Hello Bill

 Should be no problem. It's quite adaptable, but it's recommended that
 you get familiar with the standardized process first, according to
 Aleks's instructions. Then you have a solid baseline to work from in
 adapting it. One step at a time.

 I said this in an earlier message:

 One point on energy use in comparing the two main dewatering methods
 is that heating to 60-70 deg C and settling loses the heat, whereas
 with boiling it off, while using lots of energy, you can at least
 catch it on the way down and start processing the oil once it's
 cooled to 55 deg C, saving some of the extra energy. But more heat
 carries the danger of creating more FFAs, which adds to boiling being
 the less preferred method.

 It depends on the oil - will you always be working with the same oil?
 Three possibilities: nice oil, no need for dewatering; heat to 60¡C
 and settle for 24 hours, draw from the top; boil the water off. We do
 all three of those at various times. From another previous message:

 It seems heating to 60¡C and settling to separate water either works
 or it doesn't. Some people swear by it, others have no success. It
 may be due to the presence of animal fats in heavily used oils, which
 can be very difficult to remove the water content from. We've had
 mixed results. With oil from a new source we heat a sample to 100¡C
 to dewater (if any) and then process, then try the same with 60¡C and
 settling. (Or not if boiling shows there wasn't any water.)

 Best wishes

 Keith



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Re: [biofuel] Re: acid stage question

2003-05-29 Thread William Clark

Hi girl_mark,

Thanks for the help. I will be posting progress reports soon to let other
know how we are proceeding.

Good luck with your endeavors,

Bill C.
- Original Message -
From: girl_mark_fire [EMAIL PROTECTED]
To: biofuel@yahoogroups.com
Sent: Wednesday, May 28, 2003 9:22 PM
Subject: [biofuel] Re: acid stage question


 --- In biofuel@yahoogroups.com, William Clark [EMAIL PROTECTED]
 wrote:
  Hello to all.
 
  Question: If wvo is dried by boiling off water, can the acid stage
 be
  undertaken once oil temp. falls below boiling point of
 methanol?

 thats what a lot of people do


 Does higher
  temp. affect esterification in any positive or negative way?

 Faster reaction. Above 140F you'd want to be using a
 pressurised vessel so as to keep methanol liquid, or (I think)
 use a reflux mechanism in your processsor.  For homebrew I
 like using the low temp in Aleks' instructions since it works quite
 fine (the reaction speed) and I like not having to use extra energy.
 since I have that extra insulation I keep talking about, it takes very
 little electricity to heat oil to 35 C and then my processor holds
 that temperature for several hours with no additional heating.
 mark

 
  Bill C.



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[biofuel] Toyota building more low-polluting cars in and for Mexico?

2003-05-29 Thread murdoch

The picture in the paper has Mexico City with all its smog, but the
clean-air aspect of this supposed for-Mexico car is not as emphasized
in the article itself.  Of course, Toyota and other carmakers could
export EVs to Mexico City and help them that way, but that won't
happen.  Probably they'd complain about cost, and the difficulty of
generating electricity, as though every solution doesn't have
associated challenges.

Years ago I heard about the lack of Japanese car sales in Mexico, and
recently the story of Mexico losing jobs to Asia has surfaced, but I
have yet to read a story which addresses how and why the auto
companies have decided that EVs are not a decent solution to Mexico
City's notorious smog problem, nor have I seen any decent coverage of
Mexico's pretty good-sized (I think) production of ethanol, nor has
there been decent coverage of the high cost of gasoline there, despite
their status as a major producer of Oil.

http://www.signonsandiego.com/news/business/20030529-_1b29toyota.html

Company plans car made specifically for Mexico market 

By Dean Calbreath 
UNION-TRIBUNE STAFF WRITER 

May 29, 2003 



JOHN GIBBINS / Union-Tribune
Although it now does little business in Mexico, Toyota is building a
$140 million truck factory in Tijuana. The company is considering a
new car geared specificlaly for the Mexican market. 
 
TOYOTA CITY, Japan ö In the factory town that gave rise to one of the
world's most successful automakers, executives at Toyota are in the
planning stages for a new car aimed at the Mexican marketplace ö a
move that could turn Tijuana into more of an automotive hub. 

Officials from Toyota told a trade delegation from San Diego and
Tijuana last week that they are trying to design a car specifically
for Mexico. The planning stage, they say, could be finished by 2005. 

Toyota already is building a $140 million truck factory in Tijuana
that eventually will employ at least 460 workers. One motivation for
opening in Tijuana, Toyota officials say, is to boost the profile of
the company in Mexico, where it does little business. 



 
Right now, virtually no Toyota cars are selling in Mexico, said
Satoshi Tachihara, project general manager of the Americas project
division at Toyota. But there is a real need for small, low-cost,
low-polluting cars, especially in a place like Mexico City. 

Toyota officials gave no indication whether they would use the Tijuana
site as the launching pad for a Mexican car. But the news of Toyota's
plans was encouraging for the Tijuana executives among the delegation,
which was coordinated by San Diego's World Trade Center. 

I see a real future for Tijuana in the auto industry, said Jaime
Gonzalez Luna, a board member of the Tijuana Economic Development
Corp. There should be many opportunities for suppliers on both sides
of the border. 

James Roberts, who is developing a 180-acre industrial park close to
Toyota's 700-acre factory site, is banking on the idea that Toyota
will create a cluster of suppliers, parts makers, distributors and
shippers. 

Local suppliers will make Toyota more competitive in the whole scheme
of things, he said. 

Japanese auto suppliers, however, caution that Toyota's current
operation in Tijuana is too small to draw a lot of suppliers to the
region. And the lure of low-cost manufacturing in China ö coupled with
lingering concerns over the quality of Mexican auto supplies ö could
blunt the dream of an automotive boom in Tijuana. 

If Toyota's operation grows successfully, we'll have to consider
locating in Tijuana, said Tatsuya Toyoda, who heads the America team
of the international business planning group at Denso, Toyota's
biggest supplier. But we also have to consider the possibility of
China. Labor in China is less than half of that in Mexico. 

With a slew of high-tech manufacturers shutting their Mexican
production lines and shifting operations to China or other bases in
Asia, Tijuana's beleaguered maquiladora industry has been increasingly
hoping that Toyota's truck plant would lead to a new influx of
Japanese companies. 

There's good reason for their optimism. Unlike some of the electronics
firms that have been forced to pull out of Mexico because of declining
sales and profits, Toyota is a genuine moneymaker. It is the most
profitable company in Japan, with $8 billion in profits during its
recently concluded fiscal year ö a 54 percent jump over the previous
year. Roughly a third of its worldwide sales, which totaled 6.3
million vehicles last year, take place in North America. 

Toyota is currently building a plant that will start making chassis
for its Tacoma trucks next summer. By 2005, it will be assembling
entire trucks in Tijuana. Its goal is to produce 170,000 truck chassis
and 20,000 pickups a year. Teams of potential managers at the Tijuana
plant are now being trained in Toyota's headquarters in Toyota City. 

At the same time, the company ö which was beaten to the Mexican market
by such Japanese

Re: [biofuel] Two-stage Process - jelly?

2003-05-29 Thread Keith Addison

Mark, why are you using total 40% methanol - are those figures right? 
Should be half those amounts for 500cc of oil.

Dear Keith and All

Unlike some other e-mails I'll descibe exactly
what I have done.

500cc virgin vegetable oil (non-specific type)
Heated to 35'C
80cc 99.5% Methanol added
Stirred for 5 minutes
Add 0.5cc (10 drops) of 97% H2SO4
Stir at 35'C for 1 hour - 600 rpm
Stir without heat for 1 hr - 600 rpm
Settle for 8 hrs
[ At all time the vessel has been covered with
tightly fitting cling film with only a very small
hole for the thermo-couple to go in (maybe 1.5 to
2mm diameter). Methanol loss is negligable. ]

No glycerine at all. The product has not settled
but is still liquid. This is virgin oil never
used fresh from the super market ASDA here, now
owned by WoolMart.

This morning - heated the oil to 55'C. Will add
3.1g NaOH plus 120cc of Methanol. If this turns
to jelly then I will repeat again and see what
happens.

The single stage process works a treat every
time, producing good clean ME.

Keith, so the extra NaOH on top of that required
to drive the reaction neutralises the FFA's (in
used oil) and extracts them as soap in the final
wash?

In single-stage transesterification the extra NaOH on top of the base 
amount as indicated by titration neutralizes the FFAs, converting 
them to soap, which drops out as a by-product with the so-called 
glycerine layer - more like a soap layer, as Todd says. It's 
removed when you separate the biodiesel from all the gunk at the 
bottom, shouldn't be in the wash if you've done it right.

Final wash? All washes are the same, it's not that the first wash 
removes this and the second wash removes that. Each wash removes 
whatever's soluble until it gets saturated; the next wash removes 
more of the same until it too gets saturated, and so on. Well, it's 
not quite saturation, but anyway, that batch of water won't absorb 
any more junk from that batch of biodiesel. The water can be re-used 
though - see Bubblewashing 101 by Girl Mark:
http://journeytoforever.org/biodiesel_bubblewash2.html#counter

Best

Keith


Regards

Mark :-(


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Re: [biofuel] Two-stage Process - jelly?

2003-05-29 Thread mark schofield

Dear Keith

Sorry yes I used 40cc and 60cc respectively for
the process for 500cc oil not as I had previously
written. I was having a senior moment.

On the pork lard front, the single stage has
produced an extremely clean product almost the
same colour as mineral diesel here ie clear
white, if that makes sense.

So, the FFA's are neutralised and are removed
with the glycerine. The wash water then removes
the soaps that do not settle out?

Thanks Keith. I appreciate your help.

Regards

Mark

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Re: [biofuel] Two-stage Process - jelly?

2003-05-29 Thread Appal Energy

Mark,

Earlier I was curious if you were using oil or an oil/fat blend (WVO).
Should it be presumed that the feedstock at the beginning of the second
stage and prior to reheating is still liquid? If so, should it be presumed
that there was a layer of extra alcohol above the oil, perhaps slightly
darkened?

If so, and were it me, I'd separate the feedstock from such a layer and then
conduct the second stage, just to isolate variables. Second, if you're
getting jelly out of a SVO, you might wish to back off the caustic some.
Jelly, or glop soap is a condition that results from too much caustic in the
presence of water. It doesn't take much to push what is primarily a
transesterification reaction into one that is directed towards
saponification (soap making, aka jelly).

You might (or perhaps might not) care to take a look here.
http://groups.yahoo.com/group/Biodiesel/message/2504  It's a step by step
how to that runs the base side of an acid base experiment in three
separate stages, rather than all at once.

That's not to declare that it should be done in such a manner. But it does
indicate that glycerin drop in the second stage can occur with less than a
requisite amount of caustic.

Take your time and take no short cuts. It works and works well.

Todd Swearingen

- Original Message -
From: mark schofield [EMAIL PROTECTED]
To: biofuel@yahoogroups.com
Sent: Thursday, May 29, 2003 7:51 AM
Subject: Re: [biofuel] Two-stage Process - jelly?


 Dear Keith and All

 Unlike some other e-mails I'll descibe exactly
 what I have done.

 500cc virgin vegetable oil (non-specific type)
 Heated to 35'C
 80cc 99.5% Methanol added
 Stirred for 5 minutes
 Add 0.5cc (10 drops) of 97% H2SO4
 Stir at 35'C for 1 hour - 600 rpm
 Stir without heat for 1 hr - 600 rpm
 Settle for 8 hrs
 [ At all time the vessel has been covered with
 tightly fitting cling film with only a very small
 hole for the thermo-couple to go in (maybe 1.5 to
 2mm diameter). Methanol loss is negligable. ]

 No glycerine at all. The product has not settled
 but is still liquid. This is virgin oil never
 used fresh from the super market ASDA here, now
 owned by WoolMart.

 This morning - heated the oil to 55'C. Will add
 3.1g NaOH plus 120cc of Methanol. If this turns
 to jelly then I will repeat again and see what
 happens.

 The single stage process works a treat every
 time, producing good clean ME.

 Keith, so the extra NaOH on top of that required
 to drive the reaction neutralises the FFA's (in
 used oil) and extracts them as soap in the final
 wash?

 Regards

 Mark :-(


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Re: [biofuel] Diesel Boats

2003-05-29 Thread Jack Kenworthy

thanks for the input on the engine - much appreciated.  and it is not 
necessarily that I need that much power, but it is what's in the boat that is 
for sale.  It may also prove useful in hauling 1,500 lbs and ice from Eleuthera 
to the market in Nassau.
thanks again.
jack
Jack Kenworthy
Sustainable Systems Director
The Cape Eleuthera Island School
242-359-7625 ph. 954-252-2224 fax
www.islandschool.org
  - Original Message - 
  From: Neoteric Biofuels Inc 
  To: biofuel@yahoogroups.com 
  Sent: Thursday, May 29, 2003 11:55 AM
  Subject: Re: [biofuel] Diesel Boats


  Common, reliable, used in all sorts of marine applications, buses, etc.

  Known as Screaming Green Leakers I believe, for their noteworthy  
  tendency to run and run, but leak lube oil from various places.

  Just keep a rag handy.

  Pretty heavy on fuel use...my 40' tug had a Perkins 354-6, under 100HP,  
  yet could tow a small barge well, and was very economical. Do you  
  really need all that horsepower??

  Edward Beggs
  http://www.biofuels.ca


  On Thursday, May 29, 2003, at 06:09 AM, Jack Kenworthy wrote:

   I have a question for any mechanic-types out there - particularly  
   marine-diesel familiars.  I am thinking about purchasing a 40 foot  
   diesel work boat for a combined aquculture and dive operation and I am  
   wondering if any knows about:
   1 - this engine in particular:  General Motors 8V71 twin turbo rated  
   at 450 HP?  I know that GM has had some trouble with diesel engines in  
   the past just wondering if anyone has experience or knowledge  
   pertaining to this model in particular.
   2 - Special considerations for using biodiesel in marine applications?
   Thanks for the help.
   Best,
   Jack
   Jack Kenworthy
   Sustainable Systems Director
   The Cape Eleuthera Island School
   242-359-7625 ph. 954-252-2224 fax
   www.islandschool.org
  
   [Non-text portions of this message have been removed]
  
  
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[biofuel] Re: Two-stage Process - jelly?

2003-05-29 Thread girl_mark_fire

mark,
I;'m not surprised that you don't have a 'glycerine' layer after the 
first stage.
First of all, the more I think about it,  the more I doubt that it's 
glycerine you sometimes see in the bottom of the container at 
the end of the first stage- someone correct me again if I'mn 
wrong- but if it's an esterification of free fatty acids, rather than a 
transesterification of an intact triglyceride, it seems to me that 
there wouldn't be much glycerine breaking off other than the very 
small amount of trans-e that's (very slowly) occurring.  

Jon Van Gerpen's research on this process considers this layer 
to be excess methanol, combined with some water that is 
formed in the reaction. Presumably there'd also be a little bit of 
glycerine if any transesterification is happening as well, all in the 
same layer as the water/methanol.

I believe that Todd also calls it first stage methanol rather than 
first stage glycerine, and if you look at how 'runny' it is, it looks 
like methanol more than like glycerine (at least the few times Ive 
seen it). 

Van Gerpen's method (that's the exceedingly-high-methanol 
industrial process, somewhat different than Aleks' process and 
hard to do if you don't have methanol recovery and cheap energy) 
finds that depending on the amounts of methanol used and the 
amounts of water produced, the excess methanol/.water 
sometimes coalesces on top of the esters/oil, and sometimes 
ends up below the oil phase. The stuff I saw/made using his 
method created a layer that looked exactly like the watery 
'glycerine' that I've seen using A;leks' method. However I have not 
always produced this aqueous layer in Aleks;' method, and I 
frequently used that method with nice oil, just like you. So my 
guess is that it's somehow connected to the amount of water 
produced, and that the condition of the nice oil might have 
something to do with it. I would also guess that  how dry the oil is 
in the first place would be a contributing factor.
Anyway, I don't worry when I don't see first stage glycerine in 
ALeks method, as that seems quite normal to me in my 
experience. On the other hand I usually don't look for it, so it may 
appear more often than I am aware of.

Todd in the post below suggests removing any first stage 
alcohol (the dark layer, sometimes below and sometimes above 
the oils).I would add that if you do this change, be prepared to 
add a similar amount of fresh, anhydrous methanol, to replace 
any that is removed, to make sure there is enough for the 
second stage reaction. 

mark

--- In biofuel@yahoogroups.com, Appal Energy 
[EMAIL PROTECTED] wrote:
 Mark,
 
 Earlier I was curious if you were using oil or an oil/fat blend 
(WVO).
 Should it be presumed that the feedstock at the beginning of 
the second
 stage and prior to reheating is still liquid? If so, should it be 
presumed
 that there was a layer of extra alcohol above the oil, perhaps 
slightly
 darkened?
 
 If so, and were it me, I'd separate the feedstock from such a 
layer and then
 conduct the second stage, just to isolate variables. Second, if 
you're
 getting jelly out of a SVO, you might wish to back off the 
caustic some.
 Jelly, or glop soap is a condition that results from too much 
caustic in the
 presence of water. It doesn't take much to push what is 
primarily a
 transesterification reaction into one that is directed towards
 saponification (soap making, aka jelly).
 
 You might (or perhaps might not) care to take a look here.
 http://groups.yahoo.com/group/Biodiesel/message/2504  It's a 
step by step
 how to that runs the base side of an acid base experiment in 
three
 separate stages, rather than all at once.
 
 That's not to declare that it should be done in such a manner. 
But it does
 indicate that glycerin drop in the second stage can occur with 
less than a
 requisite amount of caustic.
 
 Take your time and take no short cuts. It works and works well.
 
 Todd Swearingen
 


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[biofuel] Re: [renewable-energy] OT: ad hoc comment on Astropower situation

2003-05-29 Thread murdoch

I don't have what you want, handy.  An initial attempt to search at
energy.gov yields this only slightly-helpful document and tables:

http://www.eia.doe.gov/cneaf/solar.renewables/page/rea_data/chapter2.html

The problem is in part that it has not company-specific data.

The NREL.gov website is down, which is where I'd prefer to look.

This site starts to give a manufacturer-specific and country-specific
idea:

http://www.oja-services.nl/iea-pvps/isr/31.htm

These guys want $6000 for a report containing some of the info:

http://www.kmicorp.com/photovoltaic_market_studies/pv_manufacturer.htm

I've just always liked this page:

http://www.eco-web.com/cgi-local/sfc?a=index/index.htmlb=index/category/9.1.html

Ok, so none of this helps.  I have this from a couple of years ago
that I copied down because it was a pain to get.  Not everything you
wanted, but a start on getting an idea as to the biggest:

In 1999 the six largest solar companies produced 71% of worldwide solar panel 
shipments. These six are BP Solarex, Kyocera Corp., Siemens Solar Group, Sharp 
Corp., AstroPower Inc., and Photowatt Int'l S.A. 
The top seven manufacturers accounted for about 82% of the world's PV 
shipments for 2001. They were (in approximate order) Sharp, BP Solar, Kyocera, 
Siemens Solar (recently purchased by Shell), AstroPower, RWE Solar, and 
Isofoton.



On Thu, 29 May 2003 15:02:29 -0700, you wrote:

Does anyone have an article or other summary of the state of the PV
industry at the moment?  I am not looking for one-word epithets, but a
more analytical assessment.  Like product sold worldwide, companies
showing a profit, etc.  A few years of history, with maybe one year of
projections would seem appropriate.

If you know of such a summary or summary article, and can at least
remark that it is not total B.S., I would appreciate a link or a
citation.

Thanks!

Robert Wichert



==

murdoch wrote:
 
 Over the last few months Astropower stock has collapsed.  Although I
 have allowed my indexes to be neglected, it is worth noting that at
 one time it was clearly the obvious quality amongst many alternative
 energy stocks of dubious quality, and it was a part of the
 capitalization of my ae index.
 
 It had revenues, consistent revenue growth, profits, consistent profit
 growth, etc.  They made product, they were among the world's top 15
 producers, with many oil company subsidiaries and large company
 subsidiaries competing against them, and they weren't going away.
 
 Now they have gone away, from a stock market perspective.  Their CFO
 and CEO, who was respected by others, have resigned in disgrace.  Well
 intended green-mutual-funds who invested in them have been damaged.
 
 More than one source seems to indicate that the many hundreds of lower
 workers throughout the company are not to blame, that they could
 continue to do their thing and make solar product going forward.  But
 what the heck has top management been doing to turn profits into
 losses, retroactively?  Who the hell knows.  I think it's fair to
 entertain the hypothesis that, quite simply, it is a case of fraud,
 until there's some clarification.  The company, over many months, has
 not bothered to clarify a goddamn thing.
 
 What I want to say is that, in a way, this is only too logical.  A
 couple of years ago I tried to sit down and make a list of enough
 publicly traded nearly-pure-play PV companies so that I could make a
 solar index, but it just didn't work out.  APWR was in the list of
 course, and there were a few other sort-of plays, such as SPIR, ENER,
 SWVG.F or something.
 
 Anyway, I have been thinking that some of the criticism of the Bush
 administration is shallow, and that a primary weapon of their is the
 neglect of discussion of important topics, and the neglect of the
 importance of ordering massive quantities of alternative energy
 products, rather than paying lip service to alternative energies,
 funding some research with a pittance, and then continuing the massive
 river of money to traditional energy technologies.
 
 I see the collapse of one of the only decent non-oil-company-owned
 alternative energy companies as something that the fossil fuel
 lobbyists and others probably find hysterical.  Doubtless they will
 sit around and smirk as to the corruption of those environmentalist
 jokers.
 
 One of APWRE's competitors, ENER (a subsidiary of theirs is United
 Solar, although that's only a percentage of ENER) is now part-owned by
 Chevron Texaco and I think has three or four decades of history of
 slow growth which has benefited the founder and hurt long-term
 investors irreparably.  Somehow they've always stayed afloat, perhaps
 due to those government contracts which always seem to come in.  We
 wouldn't want to perpetuate the idea that private sector demand could
 keep a PV company in business.
 
 So, APWRE is now in disgrace from a stock-market point of view, SPIR's
 solar subsidiary plods 

[biofuel] Biogas from chicken manure

2003-05-29 Thread Ackland, Tony (CALNZAS)

Does anyone have pointers re producing biogas / methane from chicken manure, 
and its subsequent use in firing heaters for nurseries ?

Tony

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