Re: [biofuel] Syngas to methanol

2004-05-20 Thread mark schofield

Walt 

Have you looked at polyethene to ethanol
reactors?

Mark  






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Re: [biofuel] Syngas to methanol

2004-05-20 Thread Walt Patrick

At 02:42 PM 5/20/04 +0100, you wrote:
 Walt
 
 Have you looked at polyethene to ethanol
 reactors?
 
 Mark

Nope. Tell us more :-)

Walt 




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Re: [biofuel] Syngas to methanol

2004-05-19 Thread mark schofield

Walt

Does you have any reference files I could look at
please?

I know that Sasol in South Africa have been using
a GTL technology via an Iron-Oxide catalyst to
produce very low sulphur diesel / petrol since
the 1950's. The catalyst is now changing over to
cobolt to reduce / prevent the formation of
waxes.

Mark






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Re: [biofuel] Syngas to methanol

2004-05-19 Thread Walt Patrick

At 09:41 AM 5/19/04 +0100, you wrote:
 Walt
 
 Does you have any reference files I could look at
 please?

Nothing that's not available on the net through google.

with best wishes,

Walt 




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Re: [biofuel] Syngas to methanol

2004-05-18 Thread Martin Klingensmith



Walt Patrick wrote:

   Currently we're undertaking to install a 100' tower and wind generator 
 in 
 order to produce quantities of H2 and O2. We're planning on using O2 
 (instead of air) to drive the thermodynamics of the conversion, and will 
 use the H2 to adjust the ratio of CO to H2 in the syngas.
 
   Hope this helps clarify what we're doing.
 
 Walt
 http://www.windward.org/
 

Walt,
are there any legal problems in doing this since it is going to be 
patented? I think it's great though, please keep us updated on how it goes.

-- 
--
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http://infoarchive.net/
http://nnytech.net/


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Re: [biofuel] Syngas to methanol

2004-05-18 Thread Walt Patrick

At 11:10 AM 5/18/04 -0400, Martin wrote:
 Walt,
 are there any legal problems in doing this since it is going to be
 patented? I think it's great though, please keep us updated on how it goes.

The research was done using a Department of Energy grant, so my 
understanding is that there's a public interest in the patent. When I spoke 
with the inventor, he didn't have a problem with us working on utilizing 
his work.

Anyone familiar with the niceties involved in public use of research 
funded by the DoE?

Walt 




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Re: [biofuel] Syngas to methanol

2004-05-18 Thread Keith Addison

At 06:46 PM 5/15/04 -0600, Greg wrote:
 Is that number correct?
 
 I get  No patents have matched your query  for 20030158270.

Sorry that I wasn't more clear. That's the patent application number; you
have to search under Published Applications, not Issued Patents.

Walt

You can find it here, in full:
http://tinyurl.com/3f5v7

That takes you straight to this unwieldy url:

http://appft1.uspto.gov/netacgi/nph-Parser?Sect1=PTO1Sect2=HITOFFd=P 
G01p=1u=%2Fnetahtml%2FPTO%2Fsrchnum.htmlr=1f=Gl=50s1=%2220030158 
270%22.PGNR.OS=DN/20030158270RS=DN/20030158270
United States Patent Application: 0030158270

United States Patent Application20030158270
Kind Code   A1
Mahajan, Devinder   August 21, 2003
Liquid phase low temperature method for production of methanol from 
synthesis gas and catalyst formulations therefor

Abstract

The invention provides a homogenous catalyst for the production of 
methanol from purified synthesis gas at low temperature and low 
pressure which includes a transition metal capable of forming 
transition metal complexes with coordinating ligands and an alkoxide, 
the catalyst dissolved in a methanol solvent system, provided the 
transition metal complex is not transition metal carbonyl. The 
coordinating ligands can be selected from the group consisting of 
N-donor ligands, P-donor ligands, O-donor ligands, C-donor ligands, 
halogens and mixtures thereof.

Etc.

Best

Keith


At 11:40 AM 5/15/04 +, you wrote:
 -
  hi walt. what do you want for the steam engine?? we want to  run one
 as an adjunct to our 25hp boiler which runs our biodiesel plant and
 distillery.we would love to use an old timey steam motor to run a
 generator..we want a cogeneration segment as part of our fuel
 production system.

   It looks like a historical association has come together to 
purchase the
steam engine and return it to it's original use, that of powering a
carousel that's maintained by a local community.

   The reason we decided to not use the old engine for the purpose you're
describing is that there are new engines available that will do the job, so
we figured that it didn't make sense to put the wear and tear on an antique.

   Consequently we replaced the 5 hp antique with a 1 hp engine 
from Mike Brown.

http://home.earthlink.net/~dlaw70/12stmng.htm

   The plan is to use a thermal battery to store heat and then use that
heat to operate the smaller steam engine 24x7. If one's primary focus is on
electrical generation, then going with a larger engine makes sense, but
when you're talking about co-generation, and the generation of electricity
is ancillary, then the smaller set up is easier to work with, develop and
control.  We're in a net metering situation, so we're just looking to
replace the electricity we use, not to try and produce a surplus.

 P,S. are you talking about destructive distillation of methanol or
 using the chips for gasification? we are fitting out  six wheel drive
 duece and a half with a chipper and a portable sawmill so we can
 implement a resource recovery program here in the Smoky mountains
 recovering bettle killed trees and recycling them

   The path we're pursuing is to convert the woodchips into 
syngas, and then
condense that into methanol.

   There have been two major developments in that area. The first involves
grinding up the zinc oxide catalyst into a powder that's slurried with
mineral oil. This allowed the through-pass conversion rates to climb from
the traditional 5% per pass to around 20%. Just as importantly, it allowed
the use of a micro reactor, i.e. the engineering tests that were used to
design the plant described in the link below was a six foot length of one
inch diameter stainless steel pipe.

http://www.lanl.gov/projects/cctc/factsheets/estmn/csliquiddemo.html

   The second involves a co-catalyst system developed by Dr. Mahajan which
allows the reaction to proceed at much reduced temperatures and pressures
(100 PSI and 150 C) The co-catalyst is also much less sensitive to the
presence of CO2 in the feed stream. This route is especially interesting
because it raises the single pass conversion rate up to better than 90%. At
that point, you can burn off the uncondensed gas and not have to worry
about the accumulation of inert gases (i.e. N2) in the reactor.

   The url for the published patent application is long so I'll 
just invite
those who are interested to go to

http://appft1.uspto.gov/netahtml/PTO/search-bool.html

and search for mahajan and methanol. The information is under patent
application number 20030158270.

   Currently we're undertaking to install a 100' tower and wind 
generator in
order to produce quantities of H2 and O2. We're planning on using O2
(instead of air) to drive the thermodynamics of the conversion, and will
use the H2 to adjust the ratio of CO to H2 in the syngas.

   Hope this helps clarify what we're doing.

Walt
http://www.windward.org/



Biofuel at Journey 

Re: [biofuel] Syngas to methanol

2004-05-16 Thread Greg Harbican

Is that number correct?  

I get  No patents have matched your query  for 20030158270.

Greg H.
  - Original Message - 
  From: Walt Patrick 
  To: biofuel@yahoogroups.com 
  Sent: Saturday, May 15, 2004 09:38
  Subject: [biofuel] Syngas to methanol


The url for the published patent application is long so I'll just 
invite 
  those who are interested to go to

  http://appft1.uspto.gov/netahtml/PTO/search-bool.html

  and search for mahajan and methanol. The information is under patent 
  application number 20030158270.




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



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Re: [biofuel] Syngas to methanol

2004-05-16 Thread Walt Patrick

At 06:46 PM 5/15/04 -0600, Greg wrote:
 Is that number correct?
 
 I get  No patents have matched your query  for 20030158270.

Sorry that I wasn't more clear. That's the patent application number; you 
have to search under Published Applications, not Issued Patents.

Walt 




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[biofuel] Syngas to methanol

2004-05-15 Thread Walt Patrick

At 11:40 AM 5/15/04 +, you wrote:
 -
  hi walt. what do you want for the steam engine?? we want to  run one
 as an adjunct to our 25hp boiler which runs our biodiesel plant and
 distillery.we would love to use an old timey steam motor to run a
 generator..we want a cogeneration segment as part of our fuel
 production system.

It looks like a historical association has come together to purchase 
the 
steam engine and return it to it's original use, that of powering a 
carousel that's maintained by a local community.

The reason we decided to not use the old engine for the purpose you're 
describing is that there are new engines available that will do the job, so 
we figured that it didn't make sense to put the wear and tear on an antique.

Consequently we replaced the 5 hp antique with a 1 hp engine from Mike 
Brown.

http://home.earthlink.net/~dlaw70/12stmng.htm

The plan is to use a thermal battery to store heat and then use that 
heat to operate the smaller steam engine 24x7. If one's primary focus is on 
electrical generation, then going with a larger engine makes sense, but 
when you're talking about co-generation, and the generation of electricity 
is ancillary, then the smaller set up is easier to work with, develop and 
control.  We're in a net metering situation, so we're just looking to 
replace the electricity we use, not to try and produce a surplus.

 P,S. are you talking about destructive distillation of methanol or
 using the chips for gasification? we are fitting out  six wheel drive
 duece and a half with a chipper and a portable sawmill so we can
 implement a resource recovery program here in the Smoky mountains
 recovering bettle killed trees and recycling them

The path we're pursuing is to convert the woodchips into syngas, and 
then 
condense that into methanol.

There have been two major developments in that area. The first involves 
grinding up the zinc oxide catalyst into a powder that's slurried with 
mineral oil. This allowed the through-pass conversion rates to climb from 
the traditional 5% per pass to around 20%. Just as importantly, it allowed 
the use of a micro reactor, i.e. the engineering tests that were used to 
design the plant described in the link below was a six foot length of one 
inch diameter stainless steel pipe.

http://www.lanl.gov/projects/cctc/factsheets/estmn/csliquiddemo.html

The second involves a co-catalyst system developed by Dr. Mahajan which 
allows the reaction to proceed at much reduced temperatures and pressures 
(100 PSI and 150 C) The co-catalyst is also much less sensitive to the 
presence of CO2 in the feed stream. This route is especially interesting 
because it raises the single pass conversion rate up to better than 90%. At 
that point, you can burn off the uncondensed gas and not have to worry 
about the accumulation of inert gases (i.e. N2) in the reactor.

The url for the published patent application is long so I'll just 
invite 
those who are interested to go to

http://appft1.uspto.gov/netahtml/PTO/search-bool.html

and search for mahajan and methanol. The information is under patent 
application number 20030158270.

Currently we're undertaking to install a 100' tower and wind generator 
in 
order to produce quantities of H2 and O2. We're planning on using O2 
(instead of air) to drive the thermodynamics of the conversion, and will 
use the H2 to adjust the ratio of CO to H2 in the syngas.

Hope this helps clarify what we're doing.

Walt
http://www.windward.org/




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