Re: [biofuels-biz] Cracking

2002-09-16 Thread Appal Energy

Lee,

Catalytic cracking is a rather involved chemical and mechanical
process, conducted under high temp and quite often high pressure.
Primary and co-products are extracted at different stages
throughout the process, using multitudes of techniques.

One look at a petrochemical facility and its multiple fractional
distillation toweres should give you an idea that, no matter what
scale the, in general the process is intensive in design.

Which puts the process in general out of the hands of shadetree
biodieselers.

Mind you, working with a simple product containing but a handful
of different esters would be far easier than a bbl of crude with
its multitudinous co-products. But the intensity of the mechnics,
processes and procedures would still be a hurdle.

I'd say that you might care to pick up a loaf sourdough and a
couple bottles of wine, then corner your favorite professor in
chemistry for a little sit down chat. Talk is usually
inexpensive. It's when you have to start buying all the
stainless, valves, fittings and vessels and putting them together
under the tutilege of a professional that the kroners start to
add up.

Todd Swearingen
- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Saturday, September 14, 2002 9:44 PM
Subject: Re: [biofuels-biz] Cracking


 So then maybe building a solar cracking unit might be a option.
What
 would be involved in cracking? Is it a just purely a heat
process.  Or
 are other factors involved? From the previous discussions it
sounded
 like an involved process or can you run a calculation that
gives you the
 right input and output yields?

 Appal Energy wrote:

 Lee,
 
 First thing? Utilize alcohols such as isopropanol and isobutyl
 rather than methanol. To what degree the process would need to
be
 altered to achieve high conversion ratios isn't clear, but
there
 would almost assuredly need to be some alterations.
 
 You could just fractionally distill the esters without any
 catalytic cracking. Shuttle your longer chain esters to
southern
 climes and the shorter chains to northern climes. But if  high
 energy inputs were put into a distillation effort, cracking
would
 probably be included just to keep the cost/yield ratio low.
 
 One could also go the route that US DOD and NREL have toyed
with,
 cryo-cooling the esters and separating them. Rumour has it
that
 this type of experimentation was being done with biodiesel so
 that it could be used at high altitudes, where the reduced
 emissions from biodiesel would contribute to con-trail
formation
 to a lesser degree than petroleum based fuels.
 
 Now if you were to ask me what I would personally do to reduce
 the gel point, it would be one of two things. The first is
 absolutely nothing,modifiying the system to accomodate that
 particular weak point of the fuel. Such modifications would
 include the usual tank heater with a few mods to forward heat
to
 the injectors and pump, a two tank system (one being but a
liter
 or two for fossil diesel) and fuel heating systems that
utilize
 both exhaust and coolant as the heating mediums.
 
 It's not uncommon in my experience to push the nose of a
vehicle
 or plane under a tent flap, where a well vented pot belly
stove
 is stoked all night. (Nights can get kinda' long north of the
 Goldstream Valley.) A few simple mods to accomodate biodiesel
 would be of considerably less overall effort.
Granted...neither
 approach is as turn key as society has come to expect.
 
 The second approach would be to start working with alternative
 alcohols. But even then, zero and sub-zero conditions (*F)
would
 still prove quite problematic.
 
 The idea of distillation and cracking is not at all attractive
 from an energy inputs perspective, but would probably become
the
 approach of choice using centralized mega-facilities, rather
 than micro. One problem there would be that the fuel is only
 seasonal, which would force such a facility to distill and
store
 fuel in advance or leave the facility without any functional
 purpose relative to biodiesel ~one-half of each year.
 
 I don't think you'll see Appal going that route unless we
could
 implement solar concentrators. Rather, we'll probably stay in
the
 right hand lane and keep travelling 55, getting wherever
everyone
 else goes in just about the same time and style.
 
 Todd Swearingen
 Appal Energy
 
 - Original Message -
 From: Lee Sheppard [EMAIL PROTECTED]
 To: biofuels-biz@yahoogroups.com
 Sent: Friday, September 13, 2002 11:26 AM
 Subject: Re: [biofuels-biz] Cracking
 
 
 
 
 Todd Swearingen so what can be done to bio-diesel to lower
the
 
 
 gel
 
 
 point? I know that adding gasoline to diesel in winter is
done
 
 
 by some
 
 
 to stop diesel gelling in winters lower temperatures.
 
 
 
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 Sponsor -~--
 
 
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Re: [biofuels-biz] Cracking

2002-09-15 Thread Steve Spence

In upstate NY, kero and diesel are sold side-by-side in most stations. Use
to work for a trucking company. Saw a few engines die because of gasoline
additions.

Steve Spence
Subscribe to the Renewable Energy Newsletter
 Discussion Boards:
http://www.green-trust.org
Renewable Energy Pages - http://www.webconx.dns2go.com/
[EMAIL PROTECTED]
- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Saturday, September 14, 2002 10:05 PM
Subject: Re: [biofuels-biz] Cracking


 Well I have not seen kerosene at truck stops. When you travel north from
 the south and you heading or in subzero weather. Just no that many
 places to pull a semi in to keep it warm or heat it backup.

 Steve Spence wrote:

 not by intelligent diesel owners. the logical choice is kerosene.
 
 Steve Spence
 Subscribe to the Renewable Energy Newsletter
  Discussion Boards:
 http://www.green-trust.org
 Renewable Energy Pages - http://www.webconx.dns2go.com/
 [EMAIL PROTECTED]
 - Original Message -
 From: Lee Sheppard [EMAIL PROTECTED]
 To: biofuels-biz@yahoogroups.com
 Sent: Friday, September 13, 2002 11:26 AM
 Subject: Re: [biofuels-biz] Cracking
 
 
 
 
 Todd Swearingen so what can be done to bio-diesel to lower the gel
 point? I know that adding gasoline to diesel in winter is done by some
 to stop diesel gelling in winters lower temperatures.
 
 
 
 
 Biofuels at Journey to Forever
 http://journeytoforever.org/biofuel.html
 Biofuel at WebConX
 http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
 List messages are archived at the Info-Archive at NNYTech:
 http://archive.nnytech.net/
 To unsubscribe from this group, send an email to:
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http://docs.yahoo.com/info/terms/
 
 
 
 
 
 
 
 
 Biofuels at Journey to Forever
 http://journeytoforever.org/biofuel.html
 Biofuel at WebConX
 http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
 List messages are archived at the Info-Archive at NNYTech:
 http://archive.nnytech.net/
 To unsubscribe from this group, send an email to:
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 Your use of Yahoo! Groups is subject to http://docs.yahoo.com/info/terms/
 
 
 
 
 
 



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



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Re: [biofuels-biz] Cracking

2002-09-14 Thread Lee Sheppard

So then maybe building a solar cracking unit might be a option. What 
would be involved in cracking? Is it a just purely a heat process.  Or 
are other factors involved? From the previous discussions it sounded 
like an involved process or can you run a calculation that gives you the 
right input and output yields?

Appal Energy wrote:

Lee,

First thing? Utilize alcohols such as isopropanol and isobutyl
rather than methanol. To what degree the process would need to be
altered to achieve high conversion ratios isn't clear, but there
would almost assuredly need to be some alterations.

You could just fractionally distill the esters without any
catalytic cracking. Shuttle your longer chain esters to southern
climes and the shorter chains to northern climes. But if  high
energy inputs were put into a distillation effort, cracking would
probably be included just to keep the cost/yield ratio low.

One could also go the route that US DOD and NREL have toyed with,
cryo-cooling the esters and separating them. Rumour has it that
this type of experimentation was being done with biodiesel so
that it could be used at high altitudes, where the reduced
emissions from biodiesel would contribute to con-trail formation
to a lesser degree than petroleum based fuels.

Now if you were to ask me what I would personally do to reduce
the gel point, it would be one of two things. The first is
absolutely nothing,modifiying the system to accomodate that
particular weak point of the fuel. Such modifications would
include the usual tank heater with a few mods to forward heat to
the injectors and pump, a two tank system (one being but a liter
or two for fossil diesel) and fuel heating systems that utilize
both exhaust and coolant as the heating mediums.

It's not uncommon in my experience to push the nose of a vehicle
or plane under a tent flap, where a well vented pot belly stove
is stoked all night. (Nights can get kinda' long north of the
Goldstream Valley.) A few simple mods to accomodate biodiesel
would be of considerably less overall effort. Granted...neither
approach is as turn key as society has come to expect.

The second approach would be to start working with alternative
alcohols. But even then, zero and sub-zero conditions (*F) would
still prove quite problematic.

The idea of distillation and cracking is not at all attractive
from an energy inputs perspective, but would probably become the
approach of choice using centralized mega-facilities, rather
than micro. One problem there would be that the fuel is only
seasonal, which would force such a facility to distill and store
fuel in advance or leave the facility without any functional
purpose relative to biodiesel ~one-half of each year.

I don't think you'll see Appal going that route unless we could
implement solar concentrators. Rather, we'll probably stay in the
right hand lane and keep travelling 55, getting wherever everyone
else goes in just about the same time and style.

Todd Swearingen
Appal Energy

- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Friday, September 13, 2002 11:26 AM
Subject: Re: [biofuels-biz] Cracking


  

Todd Swearingen so what can be done to bio-diesel to lower the


gel
  

point? I know that adding gasoline to diesel in winter is done


by some
  

to stop diesel gelling in winters lower temperatures.



 Yahoo! Groups


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Re: [biofuels-biz] Cracking

2002-09-14 Thread Lee Sheppard

Well I have not seen kerosene at truck stops. When you travel north from 
the south and you heading or in subzero weather. Just no that many 
places to pull a semi in to keep it warm or heat it backup.

Steve Spence wrote:

not by intelligent diesel owners. the logical choice is kerosene.

Steve Spence
Subscribe to the Renewable Energy Newsletter
 Discussion Boards:
http://www.green-trust.org
Renewable Energy Pages - http://www.webconx.dns2go.com/
[EMAIL PROTECTED]
- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Friday, September 13, 2002 11:26 AM
Subject: Re: [biofuels-biz] Cracking


  

Todd Swearingen so what can be done to bio-diesel to lower the gel
point? I know that adding gasoline to diesel in winter is done by some
to stop diesel gelling in winters lower temperatures.




Biofuels at Journey to Forever
http://journeytoforever.org/biofuel.html
Biofuel at WebConX
http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
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http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
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Re: [biofuels-biz] Cracking

2002-09-13 Thread Lee Sheppard


Todd Swearingen so what can be done to bio-diesel to lower the gel 
point? I know that adding gasoline to diesel in winter is done by some 
to stop diesel gelling in winters lower temperatures.



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Re: [biofuels-biz] Cracking

2002-09-13 Thread Appal Energy

Lee,

First thing? Utilize alcohols such as isopropanol and isobutyl
rather than methanol. To what degree the process would need to be
altered to achieve high conversion ratios isn't clear, but there
would almost assuredly need to be some alterations.

You could just fractionally distill the esters without any
catalytic cracking. Shuttle your longer chain esters to southern
climes and the shorter chains to northern climes. But if  high
energy inputs were put into a distillation effort, cracking would
probably be included just to keep the cost/yield ratio low.

One could also go the route that US DOD and NREL have toyed with,
cryo-cooling the esters and separating them. Rumour has it that
this type of experimentation was being done with biodiesel so
that it could be used at high altitudes, where the reduced
emissions from biodiesel would contribute to con-trail formation
to a lesser degree than petroleum based fuels.

Now if you were to ask me what I would personally do to reduce
the gel point, it would be one of two things. The first is
absolutely nothing,modifiying the system to accomodate that
particular weak point of the fuel. Such modifications would
include the usual tank heater with a few mods to forward heat to
the injectors and pump, a two tank system (one being but a liter
or two for fossil diesel) and fuel heating systems that utilize
both exhaust and coolant as the heating mediums.

It's not uncommon in my experience to push the nose of a vehicle
or plane under a tent flap, where a well vented pot belly stove
is stoked all night. (Nights can get kinda' long north of the
Goldstream Valley.) A few simple mods to accomodate biodiesel
would be of considerably less overall effort. Granted...neither
approach is as turn key as society has come to expect.

The second approach would be to start working with alternative
alcohols. But even then, zero and sub-zero conditions (*F) would
still prove quite problematic.

The idea of distillation and cracking is not at all attractive
from an energy inputs perspective, but would probably become the
approach of choice using centralized mega-facilities, rather
than micro. One problem there would be that the fuel is only
seasonal, which would force such a facility to distill and store
fuel in advance or leave the facility without any functional
purpose relative to biodiesel ~one-half of each year.

I don't think you'll see Appal going that route unless we could
implement solar concentrators. Rather, we'll probably stay in the
right hand lane and keep travelling 55, getting wherever everyone
else goes in just about the same time and style.

Todd Swearingen
Appal Energy

- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Friday, September 13, 2002 11:26 AM
Subject: Re: [biofuels-biz] Cracking



 Todd Swearingen so what can be done to bio-diesel to lower the
gel
 point? I know that adding gasoline to diesel in winter is done
by some
 to stop diesel gelling in winters lower temperatures.



  Yahoo! Groups
Sponsor -~--
 4 DVDs Free +sp Join Now
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 ---
--~-

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 http://journeytoforever.org/biofuel.html
 Biofuel at WebConX
 http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
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Re: [biofuels-biz] Cracking

2002-09-13 Thread Keith Addison

http://164.195.100.11/netacgi/nph-Parser?Sect1=PTO1Sect2=HITOFFd=PAL 
Lp=1u=/netahtml/srchnum.htmr=1f=Gl=50s1='5,713,965'.WKU.OS=PN/5 
,713,965RS=PN/5,713,965
United States Patent: 5,713,965

( 1 of 1 )

United States Patent5,713,965
Foglia ,   et al.   February 3, 1998
Production of biodiesel, lubricants and fuel and lubricant additives

Abstract

A method is described which utilizes lipases to transesterify 
triglyceride-containing substances and to esterify free fatty acids 
to alkyl esters using short chain alcohols. The alkyl esters are 
useful as alternatives or additives to automotive fuels and 
lubricants. The method is particularly advantageous because it 
utilizes inexpensive feedstocks such as animal fats, vegetable oils, 
rendered fats and restaurant grease as substrates.


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Re: [biofuels-biz] Cracking

2002-09-13 Thread Steve Spence

not by intelligent diesel owners. the logical choice is kerosene.

Steve Spence
Subscribe to the Renewable Energy Newsletter
 Discussion Boards:
http://www.green-trust.org
Renewable Energy Pages - http://www.webconx.dns2go.com/
[EMAIL PROTECTED]
- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Friday, September 13, 2002 11:26 AM
Subject: Re: [biofuels-biz] Cracking



 Todd Swearingen so what can be done to bio-diesel to lower the gel
 point? I know that adding gasoline to diesel in winter is done by some
 to stop diesel gelling in winters lower temperatures.




 Biofuels at Journey to Forever
 http://journeytoforever.org/biofuel.html
 Biofuel at WebConX
 http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
 List messages are archived at the Info-Archive at NNYTech:
 http://archive.nnytech.net/
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Re: [biofuels-biz] Cracking

2002-09-06 Thread Lee Sheppard

Well not being a chemical engineer. What would change or could change 
 the Gel point of  bio-diesel?
So is an cracking unit a heat process where layers  of  different of 
 product are produced? If  you can build a small reactor that would use 
waist products for heat to drive the process? Would you know where I 
could find plans of a reactor that could produce the right end product?
The main reason for my question is to come up with bio-diesel that wont 
gel in winter or match the petro diesel gel point.

Appal Energy wrote:

Lee,

One would think that a chemical engineer with specific training
in the petro-chemical field could clue you in.

The first low tech improvement would be to hydrogenate the
ester, cracking any double bonds using moderate pressure,
elevated temp and sufficient time. Hydrogenation would be easier
to conduct after the esterification/transesterification rather
than on the parent feedstock It would also slightly lower the
viscosity by an imperceptible amount.

And as for catalytic cracking, I would wonder exactly what
controls would have to be in place to secure a maximum carbon
chain length and what would be the ratios of co-products of
shorter lengths.

That degree of intensity would probably give cause for moving
towards centralized production and away from micro-regional, as
the process surely would warrant larger volumes in order to be
economically and energy efficient.

Something to be said for the simplicity of an acid/base reaction,
with perhaps the improvement of but hydrogenation. Both a high
pressure esterification and the hydrogenation could feasibly be
conducted in a universal reactor.

Todd Swearingen

- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Wednesday, September 04, 2002 4:00 PM
Subject: [biofuels-biz] Cracking


  

On the subject of  carbon changes and temperature. Couldn't the


oil be
  

run though a cracking unit to get the right carbon chain


length. So that
  

the diesel would gel at a lower temperature.  What would be


involved in
  

building a unit that would handle 50 to 100 gallons at a time?


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Re: [biofuels-biz] Cracking

2002-09-06 Thread Appal Energy

Lee,

Fossil fuel cracking, generally combined with fractional
distillation, is most often conducted under high temp and
pressure, under rigid conditions that can be manipulated to
derive the desired ratio of any given products. One of the tricks
is to balance the energy/economic inputs with the product outputs
so as the process is the most efficient, either from the
perspective of inputs or outputs depending upon the need. If a
person were less worried about economic efficiency and wanted or
needed to focus strictly on maximizing one product or another,
the inputs can be altered towards that side of an equation.

Still, there would be co-products. Either markets already exist
for whatever these co-products are or would have to be created in
order to keep them from becoming part of the waste stream. (Much
like coal tar used to be a part of the waste stream. Now it is
the primary constituent of the asphalt industy. Inert, they
proclaim it to be. So inert that the aromatic hydrocarbons
slowly evaporate and run off and it has to be resurfaced or
recycled on a regular basis. But that's another story. )

And yupper. The waste products probably could be used for process
heat,depending upon their emissions which may or may not be
regulated.

As for actually conducting the process? or plans for a reactor?
You or anyone would be almost entirely dependant upon the
expertise of a chemical engineer who can scratch out the
parameters and mechanics for creating the end product you wish.

That's why I suggested and we're experimenting with simple
processes such as hydrogenation and HTP esterification - single
end-product reactions. These can be conducted in a small system
with relative ease and safety without requiring too much
technical input, using the same vessel for either process.

Mind you that this is not to suggest that a hydrogenation
reaction should be conducted in a zero lot line subdivision in
one's garage, as sooner or later some yeah hoo would attempt to
use direct flame heat in a system and blow the garage apart with
a hydrogen explosion.
!! ___B-O-O-M !!!

In any event, these processes only improve total ester yields and
increase the energy content (hydrogenation breaks double bonds).
You would still be left with a fuel that has a higher gel point
than D-1 or D-2, running about 13.77 carbons. Rapeseed methyl
ester has an average carbon chain length of ~19.96 while soybean
methyl ester averages ~16.16.

It would be interesting to get viscosity stats of these and other
methyl esters, including those derived strictly from isolated
fatty acids, for comparison of cloud points.

The following are the chemical formulas of the primary fatty
acids that are constituents of parent oils.

Butyric - C4H8O2
Caproic - C6H12O2
Capric - C10H20O2
Lauric - C12H24O2
Myristic - C14H28O2
Palmitic - C16H32O2
Linoleic -C18H32O2
Linolenic - C18H_O_
Oleic - C18H34O2
Stearic - C18H36O2
Ricinoleic - C18H34O3
Eruicic -  C22H42O2

Todd Swearingen

- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Friday, September 06, 2002 11:03 AM
Subject: Re: [biofuels-biz] Cracking


 Well not being a chemical engineer. What would change or could
change
  the Gel point of  bio-diesel?
 So is an cracking unit a heat process where layers  of
different of
  product are produced? If  you can build a small reactor that
would use
 waist products for heat to drive the process? Would you know
where I
 could find plans of a reactor that could produce the right end
product?
 The main reason for my question is to come up with bio-diesel
that wont
 gel in winter or match the petro diesel gel point.

 Appal Energy wrote:

 Lee,
 
 One would think that a chemical engineer with specific
training
 in the petro-chemical field could clue you in.
 
 The first low tech improvement would be to hydrogenate the
 ester, cracking any double bonds using moderate pressure,
 elevated temp and sufficient time. Hydrogenation would be
easier
 to conduct after the esterification/transesterification rather
 than on the parent feedstock It would also slightly lower the
 viscosity by an imperceptible amount.
 
 And as for catalytic cracking, I would wonder exactly what
 controls would have to be in place to secure a maximum carbon
 chain length and what would be the ratios of co-products of
 shorter lengths.
 
 That degree of intensity would probably give cause for moving
 towards centralized production and away from micro-regional,
as
 the process surely would warrant larger volumes in order to be
 economically and energy efficient.
 
 Something to be said for the simplicity of an acid/base
reaction,
 with perhaps the improvement of but hydrogenation. Both a high
 pressure esterification and the hydrogenation could feasibly
be
 conducted in a universal reactor.
 
 Todd Swearingen
 
 - Original Message -
 From: Lee Sheppard [EMAIL PROTECTED]
 To: biofuels-biz@yahoogroups.com
 Sent: Wednesday

Re: [biofuels-biz] Cracking

2002-09-05 Thread Appal Energy

Lee,

One would think that a chemical engineer with specific training
in the petro-chemical field could clue you in.

The first low tech improvement would be to hydrogenate the
ester, cracking any double bonds using moderate pressure,
elevated temp and sufficient time. Hydrogenation would be easier
to conduct after the esterification/transesterification rather
than on the parent feedstock It would also slightly lower the
viscosity by an imperceptible amount.

And as for catalytic cracking, I would wonder exactly what
controls would have to be in place to secure a maximum carbon
chain length and what would be the ratios of co-products of
shorter lengths.

That degree of intensity would probably give cause for moving
towards centralized production and away from micro-regional, as
the process surely would warrant larger volumes in order to be
economically and energy efficient.

Something to be said for the simplicity of an acid/base reaction,
with perhaps the improvement of but hydrogenation. Both a high
pressure esterification and the hydrogenation could feasibly be
conducted in a universal reactor.

Todd Swearingen

- Original Message -
From: Lee Sheppard [EMAIL PROTECTED]
To: biofuels-biz@yahoogroups.com
Sent: Wednesday, September 04, 2002 4:00 PM
Subject: [biofuels-biz] Cracking


 On the subject of  carbon changes and temperature. Couldn't the
oil be
 run though a cracking unit to get the right carbon chain
length. So that
 the diesel would gel at a lower temperature.  What would be
involved in
 building a unit that would handle 50 to 100 gallons at a time?


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 http://journeytoforever.org/biofuel.html
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 http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
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[biofuels-biz] Cracking

2002-09-04 Thread Lee Sheppard

On the subject of  carbon changes and temperature. Couldn't the oil be 
run though a cracking unit to get the right carbon chain length. So that 
the diesel would gel at a lower temperature.  What would be involved in 
building a unit that would handle 50 to 100 gallons at a time?  


 Yahoo! Groups Sponsor -~--
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http://www.webconx.dns2go.com/2000/biofuel/biofuel.htm
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