Re: [biofuel] continuous process plans

2003-08-21 Thread Alan Petrillo

Appal Energy wrote:
>>I haven't looked at a comparison much, myself.  I'm building a
>>continuous processor more because I want to than for any other reason.
> 
> 
> Well, when you get the thing duct taped together, installed in an explosion
> proof bunker and ready to test, we ought to run some side by sides, cradle
> to grave.

Nah, duct tape leaks too much.  Silicone and epoxy are better options.

Duct tape, safety wire, epoxy, silicone, and chewing gum do figure 
prominently in a lot of my projects, though.

And the need for fire supression had crossed my mind.  The first 
precaution there is to have adequate ventilation so that flamable vapors 
don't build up to explosive levels.


AP



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Re: [biofuel] continuous process plans

2003-08-20 Thread Appal Energy

> I haven't looked at a comparison much, myself.  I'm building a
> continuous processor more because I want to than for any other reason.

Well, when you get the thing duct taped together, installed in an explosion
proof bunker and ready to test, we ought to run some side by sides, cradle
to grave.

Todd Swearingen

- Original Message -
From: "Alan Petrillo" <[EMAIL PROTECTED]>
To: 
Sent: Wednesday, August 20, 2003 1:37 AM
Subject: Re: [biofuel] continuous process plans


> Hello, Todd.
>
> Appal Energy wrote:
> > Alan,
> >
> > Call me a dinosaur, or just one who has narrowed his focus to the near
> > exclusion of continuous processing, but what is OFM?
>
> Oh, sorry.  Oscillatory Flow Mixer.
>
> http://www.cheng.cam.ac.uk/groups/polymer/OFM/index.html
>
> Basically, it's an easy way to mix liquids moving through a pipe.
>
> > Never been overly thrilled with CP, unless it's cold processing. But
then
> > that's the old soap maker in me.
>
> It's right up there with hard milling.  :-)
>
> > Just seems to me that if one has to battle "in transit residence times,"
or
> > better still high temperature and pressure in order to get a quality
> > finished product, then it is far simpler to go with batch processing of
> > similar capacity.
>
> Residence times are easy to deal with.  It's that high pressure stuff
> that's difficult.  That's why I don't bother with it.  To much effort
> for a hobbiest like myself.
>
> > I have to ask, partly because I've not fixated on CP and in all do
> > seriousness, who has done any side by side examination of system sizes,
> > production volume, energy efficiency, quality and cost between the two
types
> > of processing systems?
>
> I haven't looked at a comparison much, myself.  I'm building a
> continuous processor more because I want to than for any other reason.
>
> > High temp and pressure for transient fluids don't appear to be a simple
> > exercise in fall canning conducted in the summer kitchen.
>
> Definitely not.
>
>
> AP
>
>
>
>
>
>
> Biofuel at Journey to Forever:
> http://journeytoforever.org/biofuel.html
>
> Biofuels list archives:
> http://archive.nnytech.net/
>
> Please do NOT send Unsubscribe messages to the list address.
> To unsubscribe, send an email to:
> [EMAIL PROTECTED]
>
> Your use of Yahoo! Groups is subject to http://docs.yahoo.com/info/terms/
>
>
>


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Re: [biofuel] continuous process plans

2003-08-20 Thread Keith Addison

Hello Andreas

Thanks for the tif's - I hope to work on them tonight.

>Keith, Thomas,...
>
>one of the main ideas behind the countercurrent contiuous reactor is to use
>extraction instead of evaporization to recover the alcohol. To do so we
>probably need some data about solubility (e.g. Methanol in WVO /
>Biodiesel,...).
>
>Does anyone know where to get those data?

I found you can blend up to 21% absolute ethanol with virgin canola 
and it stays mixed, and 5% water content in the ethanol (as per 
ACREVO) didn't make much if any difference. Only up to 13% absolute 
methanol, by contrast. Not sure about biodiesel, but the methanol 
prefers the glycerine to the biodiesel.

Best

Keith


>Andreas Ohnsorge
>
>CSC Ploenzke AG
>Abraham-Lincoln-Park 1
>65189 Wiesbaden
>Germany
>Phone: +49.611.142.20020
>Fax: +49.611.142.980028
>Mobile:+49 172 - 8 43 30 32
>e-Mail: [EMAIL PROTECTED]
>Internet: http://www.de.csc.com
>
>100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
>in der Team-Gesamtwertung http://www.csc-cycling.com/.
>
>
>- 
>---
>
>This is a PRIVATE message. If you are not the intended recipient, please
>delete without copying and kindly advise us by e-mail of the mistake in
>delivery. NOTE: Regardless of content, this e-mail shall not operate to
>bind CSC to any order or other contract unless pursuant to explicit written
>agreement or government initiative expressly permitting the use of e-mail
>for such purpose.
>- 
>---
>
>
>
>
> 
>
>  Keith Addison 
>
>      biofuel@yahoogroups.com 
>
>      @journeytoforeve cc: 
>
>  r.org>   Subject: Re: 
>[biofuel] continuous process plans 
>
> 
>
>  15.08.2003 23:19 
>
>  Please respond 
>
>  to biofuel 
>
> 
>
> 
>
>
>
>
>
>Hello Andreas, Tomas and all
>
> >Tomas,
> >
> >I am currently on some similar route - I had some experience with batch
> >process and am about to construct a continuous processor following a
>Patent
> >from Metallgesellschaft out of 1985. Could explain a bit the basis of your
> >process / could you give me your email address I really would like to get
> >in contact with you and discuss the approaches...
> >
> >How do you think?
>
>I think it would be much better if you discussed it on-list instead
>of privately, so that everyone could share in and hopefully
>contribute to the discussion.
>
>Best wishes
>
>Keith Addison
>Journey to Forever
>
> >
> >Andreas Ohnsorge
> >
> >CSC Ploenzke AG
> >Abraham-Lincoln-Park 1
> >65189 Wiesbaden
> >Germany
> >Phone: +49.611.142.20020
> >Fax: +49.611.142.980028
> >Mobile:+49 172 - 8 43 30 32
> >e-Mail: [EMAIL PROTECTED]
> >Internet: http://www.de.csc.com
> >
> >100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
> >in der Team-Gesamtwertung http://www.csc-cycling.com/.
> >
> >
> >-
> >---
> >
> >This is a PRIVATE message. If you are not the intended recipient, please
> >delete without copying and kindly advise us by e-mail of the mistake in
> >delivery. NOTE: Regardless of content, this e-mail shall not operate to
> >bind CSC to any order or other contract unless pursuant to explicit
>written
> >agreement or government initiative expressly permitting the use of e-mail
> >for such purpose.
> >-
> >---
> >
> >
> >
> >
> >
> >
> >  Johnsson Tomas
> >
> >   >"'biofuel@yahoogroups.com'" 
> >
> >  @pohjola.fi> cc:
> >
> >   Subject: [biofuel]
> >continuous process plans
> >  15.08.2003 09:10
> >
> >  Please respond
> >
> >  to biofuel
> >
> >
> >
> >
> >
> >
> >
> >
> >
> >Hello All,
> >
> >During long nights of batch processing BD the idea of building a
>continuous
> >process has been born. The first ideas is to make a stan

Re: [biofuel] continuous process plans

2003-08-20 Thread Andreas W Ohnsorge


Keith, Thomas,...

one of the main ideas behind the countercurrent contiuous reactor is to use
extraction instead of evaporization to recover the alcohol. To do so we
probably need some data about solubility (e.g. Methanol in WVO /
Biodiesel,...).

Does anyone know where to get those data?



Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
delete without copying and kindly advise us by e-mail of the mistake in
delivery. NOTE: Regardless of content, this e-mail shall not operate to
bind CSC to any order or other contract unless pursuant to explicit written
agreement or government initiative expressly permitting the use of e-mail
for such purpose.






   
  Keith Addison 
   
 Subject: Re: [biofuel] 
continuous process plans 

   
  15.08.2003 23:19  
   
  Please respond
   
  to biofuel
   

   

   




Hello Andreas, Tomas and all

>Tomas,
>
>I am currently on some similar route - I had some experience with batch
>process and am about to construct a continuous processor following a
Patent
>from Metallgesellschaft out of 1985. Could explain a bit the basis of your
>process / could you give me your email address I really would like to get
>in contact with you and discuss the approaches...
>
>How do you think?

I think it would be much better if you discussed it on-list instead
of privately, so that everyone could share in and hopefully
contribute to the discussion.

Best wishes

Keith Addison
Journey to Forever

>
>Andreas Ohnsorge
>
>CSC Ploenzke AG
>Abraham-Lincoln-Park 1
>65189 Wiesbaden
>Germany
>Phone: +49.611.142.20020
>Fax: +49.611.142.980028
>Mobile:+49 172 - 8 43 30 32
>e-Mail: [EMAIL PROTECTED]
>Internet: http://www.de.csc.com
>
>100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
>in der Team-Gesamtwertung http://www.csc-cycling.com/.
>
>
>-
>---
>
>This is a PRIVATE message. If you are not the intended recipient, please
>delete without copying and kindly advise us by e-mail of the mistake in
>delivery. NOTE: Regardless of content, this e-mail shall not operate to
>bind CSC to any order or other contract unless pursuant to explicit
written
>agreement or government initiative expressly permitting the use of e-mail
>for such purpose.
>-
>---
>
>
>
>
>
>
>  Johnsson Tomas
>
>  "'biofuel@yahoogroups.com'" 
>
>  @pohjola.fi> cc:
>
>   Subject: [biofuel]
>continuous process plans
>  15.08.2003 09:10
>
>  Please respond
>
>  to biofuel
>
>
>
>
>
>
>
>
>
>Hello All,
>
>During long nights of batch processing BD the idea of building a
continuous
>process has been born. The first ideas is to make a standing
>oscilatorprocessor. The feeding of the catalyt and the oil we are planning
>to do with hose pumps. The pumps by it self has a 1% accuracy and by
>keeping
>the oil at same temperature before feeding it throu

Re: [biofuel] continuous process plans

2003-08-20 Thread Alan Petrillo

Hello, Todd.

Appal Energy wrote:
> Alan,
> 
> Call me a dinosaur, or just one who has narrowed his focus to the near
> exclusion of continuous processing, but what is OFM?

Oh, sorry.  Oscillatory Flow Mixer.

http://www.cheng.cam.ac.uk/groups/polymer/OFM/index.html

Basically, it's an easy way to mix liquids moving through a pipe.

> Never been overly thrilled with CP, unless it's cold processing. But then
> that's the old soap maker in me.

It's right up there with hard milling.  :-)

> Just seems to me that if one has to battle "in transit residence times," or
> better still high temperature and pressure in order to get a quality
> finished product, then it is far simpler to go with batch processing of
> similar capacity.

Residence times are easy to deal with.  It's that high pressure stuff 
that's difficult.  That's why I don't bother with it.  To much effort 
for a hobbiest like myself.

> I have to ask, partly because I've not fixated on CP and in all do
> seriousness, who has done any side by side examination of system sizes,
> production volume, energy efficiency, quality and cost between the two types
> of processing systems?

I haven't looked at a comparison much, myself.  I'm building a 
continuous processor more because I want to than for any other reason.

> High temp and pressure for transient fluids don't appear to be a simple
> exercise in fall canning conducted in the summer kitchen.

Definitely not.


AP





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Re: [biofuel] continuous process plans

2003-08-19 Thread Appal Energy

Alan,

Call me a dinosaur, or just one who has narrowed his focus to the near
exclusion of continuous processing, but what is OFM?

Never been overly thrilled with CP, unless it's cold processing. But then
that's the old soap maker in me.

Just seems to me that if one has to battle "in transit residence times," or
better still high temperature and pressure in order to get a quality
finished product, then it is far simpler to go with batch processing of
similar capacity.

I have to ask, partly because I've not fixated on CP and in all do
seriousness, who has done any side by side examination of system sizes,
production volume, energy efficiency, quality and cost between the two types
of processing systems?

High temp and pressure for transient fluids don't appear to be a simple
exercise in fall canning conducted in the summer kitchen.

Todd Swearingen

- Original Message -
From: "Alan Petrillo" <[EMAIL PROTECTED]>
To: 
Sent: Tuesday, August 19, 2003 9:37 AM
Subject: Re: [biofuel] continuous process plans


> Appal Energy wrote:
> >>>A major disadvantage, I think, would be that continuous processors
> >>>are not suitable for two-stage processes, is that right?
> >>
> >>Well, yes and no.  What you have to do, effectively, is to build two
> >>processors.  One for the acid stage and a second one for the base stage.
> >
> >
> > Well, yes and no. You only have to build or install "two" processors if
the
> > need is to improve the production volume. Otherwise the same processor
can
> > be used on the first day for the acid stage and the second day for the
base
> > side - ~3.5 cycles per week, opposed to ~7 cycles per week running
straight
> > base.
>
> Good point.  Cycle it through the acid stage and then into a
> holding/settling tank, then cycle it through again for the base stage.
> Yes, with a little extra plumbing, that'd be doable.  It wouldn't be
> truly "continuous", but so what?  That way you don't have to build a
> second OFM.
>
> Come to think of it, isn't this what the people building the automatic
> single tank processors are doing, basically?  That way you don't have to
> build an OFM at all, just use a tank.
>
> Hmmm...
>
>
> AP
>
>
>
> Biofuel at Journey to Forever:
> http://journeytoforever.org/biofuel.html
>
> Biofuels list archives:
> http://archive.nnytech.net/
>
> Please do NOT send Unsubscribe messages to the list address.
> To unsubscribe, send an email to:
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>
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>
>
>


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RE: [biofuel] continuous process plans

2003-08-19 Thread Keith Addison

>Yup.
>And the files section is shut of for users to use?
>
>Johs.

Hi Johs

No, it's not shut off. Users can access it and download whatever they 
might find there, FWIW, but they can't upload. And, as explained, 
only list members can access it at all now, and only when logged in 
at Yahoo.

Best

Keith



> > -Original Message-
> > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > Sent: 18. august 2003 22:40
> > To: biofuel@yahoogroups.com
> > Subject: RE: [biofuel] continuous process plans
> >
> > Hi Johs
> >
> > >Upload it to the files section?
> >
> > Trouble is Yahoo's just changed the rules, and Files sections are now
> > only accessible to list members - okay, so we're all list members
> > here, but you'd have to sign in at Yahoo first with username and ID,
> > which quite a number of email subscription members have had problems
> > with. Then they complain to me, and I really don't have the time to
> > help people struggle with Yahoo. (I speak from experience.) I reckon
> > the Files section's virtually useless now.
> >
> > I might be able to arrange something better, if Andreas emails me
> > with details of the tif file.
> >
> > Best
> >
> > Keith
> >
> >
> >
> >
> > > > -Original Message-
> > > > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > > > Sent: 18. august 2003 21:32
> > > > To: biofuel@yahoogroups.com
> > > > Subject: Re: [biofuel] continuous process plans
> > > >
> > > > >Andrew,
> > > > >
> > > > >it seems I cannot attach anything to my emails. Would you like to
> > >give me
> > > > >your email-address that I can send you the patent as a tif-file?
> > > >
> > > > The list doesn't accept attachments, as an essential anti-virus
> > > > measure. Please contact me off-list about this, I can probably
> > > > arrange something suitable.


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RE: [biofuel] continuous process plans

2003-08-19 Thread Keith Addison

>Keith,
>
>I'd like to do so - what is the address I should send the file to?
>
>
>
>Andreas Ohnsorge

Hi Andreas

Send it straight to me:
[EMAIL PROTECTED]

Thanks!

Keith


>CSC Ploenzke AG
>Abraham-Lincoln-Park 1
>65189 Wiesbaden
>Germany
>Phone: +49.611.142.20020
>Fax: +49.611.142.980028
>Mobile:+49 172 - 8 43 30 32
>e-Mail: [EMAIL PROTECTED]
>Internet: http://www.de.csc.com
>
>100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
>in der Team-Gesamtwertung http://www.csc-cycling.com/.
>
>  Keith Addison 
>
>  biofuel@yahoogroups.com 
>
>  @journeytoforeve     cc: 
>
>  r.org>   Subject: RE: 
>[biofuel] continuous process plans 
>
> 
>
>  18.08.2003 22:39 
>
>  Please respond 
>
>  to biofuel 
>
> 
>
> 
>
>
>
>
>
>Hi Johs
>
> >Upload it to the files section?
>
>Trouble is Yahoo's just changed the rules, and Files sections are now
>only accessible to list members - okay, so we're all list members
>here, but you'd have to sign in at Yahoo first with username and ID,
>which quite a number of email subscription members have had problems
>with. Then they complain to me, and I really don't have the time to
>help people struggle with Yahoo. (I speak from experience.) I reckon
>the Files section's virtually useless now.
>
>I might be able to arrange something better, if Andreas emails me
>with details of the tif file.
>
>Best
>
>Keith
>
>
>
>
> > > -Original Message-
> > > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > > Sent: 18. august 2003 21:32
> > > To: biofuel@yahoogroups.com
> > > Subject: Re: [biofuel] continuous process plans
> > >
> > > >Andrew,
> > > >
> > > >it seems I cannot attach anything to my emails. Would you like to
> >give me
> > > >your email-address that I can send you the patent as a tif-file?
> > >
> > > The list doesn't accept attachments, as an essential anti-virus
> > > measure. Please contact me off-list about this, I can probably
> > > arrange something suitable.
 


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Re: [biofuel] continuous process plans

2003-08-19 Thread Alan Petrillo

Appal Energy wrote:
>>>A major disadvantage, I think, would be that continuous processors
>>>are not suitable for two-stage processes, is that right?
>>
>>Well, yes and no.  What you have to do, effectively, is to build two
>>processors.  One for the acid stage and a second one for the base stage.
> 
> 
> Well, yes and no. You only have to build or install "two" processors if the
> need is to improve the production volume. Otherwise the same processor can
> be used on the first day for the acid stage and the second day for the base
> side - ~3.5 cycles per week, opposed to ~7 cycles per week running straight
> base.

Good point.  Cycle it through the acid stage and then into a 
holding/settling tank, then cycle it through again for the base stage. 
Yes, with a little extra plumbing, that'd be doable.  It wouldn't be 
truly "continuous", but so what?  That way you don't have to build a 
second OFM.

Come to think of it, isn't this what the people building the automatic 
single tank processors are doing, basically?  That way you don't have to 
build an OFM at all, just use a tank.

Hmmm...


AP


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RE: [biofuel] continuous process plans

2003-08-19 Thread Johs Kleppe

Yup.
And the files section is shut of for users to use?

Johs.

> -Original Message-
> From: Keith Addison [mailto:[EMAIL PROTECTED]
> Sent: 18. august 2003 22:40
> To: biofuel@yahoogroups.com
> Subject: RE: [biofuel] continuous process plans
> 
> Hi Johs
> 
> >Upload it to the files section?
> 
> Trouble is Yahoo's just changed the rules, and Files sections are now
> only accessible to list members - okay, so we're all list members
> here, but you'd have to sign in at Yahoo first with username and ID,
> which quite a number of email subscription members have had problems
> with. Then they complain to me, and I really don't have the time to
> help people struggle with Yahoo. (I speak from experience.) I reckon
> the Files section's virtually useless now.
> 
> I might be able to arrange something better, if Andreas emails me
> with details of the tif file.
> 
> Best
> 
> Keith
> 
> 
> 
> 
> > > -Original Message-
> > > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > > Sent: 18. august 2003 21:32
> > > To: biofuel@yahoogroups.com
> > > Subject: Re: [biofuel] continuous process plans
> > >
> > > >Andrew,
> > > >
> > > >it seems I cannot attach anything to my emails. Would you like to
> >give me
> > > >your email-address that I can send you the patent as a tif-file?
> > >
> > > The list doesn't accept attachments, as an essential anti-virus
> > > measure. Please contact me off-list about this, I can probably
> > > arrange something suitable.
> 
> 
>  Yahoo! Groups Sponsor
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> 





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Re: [biofuel] continuous process plans

2003-08-19 Thread Appal Energy

> > A major disadvantage, I think, would be that continuous processors
> > are not suitable for two-stage processes, is that right?
>
> Well, yes and no.  What you have to do, effectively, is to build two
> processors.  One for the acid stage and a second one for the base stage.

Well, yes and no. You only have to build or install "two" processors if the
need is to improve the production volume. Otherwise the same processor can
be used on the first day for the acid stage and the second day for the base
side - ~3.5 cycles per week, opposed to ~7 cycles per week running straight
base.

Todd Swearingen


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RE: [biofuel] continuous process plans

2003-08-19 Thread Andreas W Ohnsorge


Keith,

I'd like to do so - what is the address I should send the file to?



Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




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delete without copying and kindly advise us by e-mail of the mistake in
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  Keith Addison 
   
 Subject: RE: [biofuel] 
continuous process plans 

   
  18.08.2003 22:39  
   
  Please respond
   
  to biofuel
   

   

   




Hi Johs

>Upload it to the files section?

Trouble is Yahoo's just changed the rules, and Files sections are now
only accessible to list members - okay, so we're all list members
here, but you'd have to sign in at Yahoo first with username and ID,
which quite a number of email subscription members have had problems
with. Then they complain to me, and I really don't have the time to
help people struggle with Yahoo. (I speak from experience.) I reckon
the Files section's virtually useless now.

I might be able to arrange something better, if Andreas emails me
with details of the tif file.

Best

Keith




> > -Original Message-
> > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > Sent: 18. august 2003 21:32
> > To: biofuel@yahoogroups.com
> > Subject: Re: [biofuel] continuous process plans
> >
> > >Andrew,
> > >
> > >it seems I cannot attach anything to my emails. Would you like to
>give me
> > >your email-address that I can send you the patent as a tif-file?
> >
> > The list doesn't accept attachments, as an essential anti-virus
> > measure. Please contact me off-list about this, I can probably
> > arrange something suitable.



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Re: [biofuel] continuous process plans

2003-08-18 Thread Alan Petrillo

J Allen wrote:
> Guy you can go through a company call micro motion they make pump and 
> meters that once are set they will deliver the amount you want and need. 
> Jim Allen

I found Micro Motion, as a subsidiary of Emerson Process, but all I saw 
there was meters, not pumps.  Do you have a link to more of their 
products?


AP


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Re: [biofuel] continuous process plans

2003-08-18 Thread Alan Petrillo

Keith Addison wrote:
> Hello Andreas, Tomas
>> - The reactor size can be much smaller (only a couple of litres
>>instead of 55 gallons...) and thus better fits in the basement of my
>>house...
> 
> 
> Yes, an advantage perhaps, depending on circumstances.
> 
> A major disadvantage, I think, would be that continuous processors 
> are not suitable for two-stage processes, is that right?

Well, yes and no.  What you have to do, effectively, is to build two 
processors.  One for the acid stage and a second one for the base stage.

In the current design of my partially built continuous processor I 
intended to automate the base/base two stage method.  My original intent 
was to run the first stage through an OFM, then through a 
coalescer/separator, and then into a second OFM for the second stage.  I 
  immagine the acid/base process could be run the same way, omitting the 
coalescer/separator in the middle.


AP



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RE: [biofuel] continuous process plans

2003-08-18 Thread Keith Addison

Hi Johs

>Upload it to the files section?

Trouble is Yahoo's just changed the rules, and Files sections are now 
only accessible to list members - okay, so we're all list members 
here, but you'd have to sign in at Yahoo first with username and ID, 
which quite a number of email subscription members have had problems 
with. Then they complain to me, and I really don't have the time to 
help people struggle with Yahoo. (I speak from experience.) I reckon 
the Files section's virtually useless now.

I might be able to arrange something better, if Andreas emails me 
with details of the tif file.

Best

Keith




> > -Original Message-
> > From: Keith Addison [mailto:[EMAIL PROTECTED]
> > Sent: 18. august 2003 21:32
> > To: biofuel@yahoogroups.com
> > Subject: Re: [biofuel] continuous process plans
> >
> > >Andrew,
> > >
> > >it seems I cannot attach anything to my emails. Would you like to
>give me
> > >your email-address that I can send you the patent as a tif-file?
> >
> > The list doesn't accept attachments, as an essential anti-virus
> > measure. Please contact me off-list about this, I can probably
> > arrange something suitable.


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RE: [biofuel] continuous process plans

2003-08-18 Thread Johs Kleppe

Upload it to the files section?



> -Original Message-
> From: Keith Addison [mailto:[EMAIL PROTECTED]
> Sent: 18. august 2003 21:32
> To: biofuel@yahoogroups.com
> Subject: Re: [biofuel] continuous process plans
> 
> >Andrew,
> >
> >it seems I cannot attach anything to my emails. Would you like to
give me
> >your email-address that I can send you the patent as a tif-file?
> 
> The list doesn't accept attachments, as an essential anti-virus
> measure. Please contact me off-list about this, I can probably
> arrange something suitable.





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Re: [biofuel] continuous process plans

2003-08-18 Thread Keith Addison

Hello Andreas, Tomas

>Keith, Thomas,
>
>I mentioned the continuous approach in a comment beginning of July (see
>attached email conversation) and out of your response (Keith) I got the
>impression that this is not very interesting for the forum. May be this is
>a misunderstanding and I would like to be convinced that it is.

I think it might be a double misunderstanding. What I disagreed with 
was your statement that batch-type processors are not suitable for 
equilibrium-type reactions, which is clearly untrue, as simple 
batch-type processors are proven to be fully capable of producing 
biodiesel that is well within the various national standards 
specifications. I would also not agree that the continuous, pipe-type 
processor would produce better results. But I didn't say that it 
would produce worse results, nor that it was of no interest here. 
Obviously there is interest here, and I did say that several people 
were working with this approach successfully. I also said this:

>confident that they'll deliver the goods in good order in due 
>course. I know there's also been much ado about continuous reactors 
>at another forum, FWIW, but I haven't taken any notice, not very 
>interested.

It's that particular forum and what goes on there that fail to 
interest me, not the continuous processors. Sorry if you found that 
confusing.

I'm a bit puzzled by the sequence of previous messages in your post, 
it seems to be a combination of messages from several threads, with 
some preceding messages missing, such as the one in which you made 
the statement about batch-type processors, though my reply to it is 
there. So I'll post both messages again here now to clear up any 
confusion:

>Subject: Re: [biofuel] Biodiesel reaction / reactor type
>
>>Reading the reasoning behind the two stage process approach it seems to me
>>that the benefit lies in the two different equilibrium points (first stage
>>mass conversion to biodiesel and second stage the -more or less - 100%
>>completion of that conversion). Am I right so far?
>>
>>If this is correct then I do remember my university time that there were
>>two different types of reactors to be used: The batch stirred vessel type
>>that is usually described here and the pipe-type where the reactants flow
>>through a pipe, ususally in different directions. If I remember right the
>>vessel is not good for beeing used in equilibrium state reactions (like
>>assumed here) - it should be preferred for quick reactions that easily
>>reach the 100% end.
>>
>>Taking this into account the better reactor type for our biodiesel rection
>>would be the pipe. Does anyone have any experience in using a pipe-type
>>reactor for producing biodiesel? I think it could easily be built using
>>plastic waste water pipes filles with glas or other inert media and mixed
>>with pulse-pumps (membrane type for example). It would also have the
>>advantage of continuous production
>>
>>Any thoughts about this approach?
>>
>>Andreas Ohnsorge
>
>
>Hello Andreas
>
>I think this is the wrong way round:
>
>>... (first stage
>>mass conversion to biodiesel and second stage the -more or less - 100%
>>completion of that conversion).
>
>It's in the second stage that there's mass conversion to biodiesel. 
>Of course 100% completion is not ever achieved. The goal is to 
>arrive within the limitations set by the various international 
>standards, and the processes available to us now are proven to be 
>more than capable of achieving that.
>
>I think your conclusions about different types of reactors might 
>apply in laboratory conditions where accurate research results are 
>important, or in industry at large scale perhaps, but for 
>homebrewers and small-scale local producers at least, and probably 
>well beyond that, there isn't any need: the  batch-type stirred and 
>heated processors now in wide use are cheap, simple and effective.
>
>FYI, there's a continuous reactor design here:
>http://journeytoforever.org/biodiesel_processor.html#continuous
>
>Some people we know are working successfully with small-scale 
>continuous designs but they're not ready to talk about it yet. 
>Judging by their track record I'd be confident that they'll deliver 
>the goods in good order in due course. I know there's also been much 
>ado about continuous reactors at another forum, FWIW, but I haven't 
>taken any notice, not very interested.
>
>Best wishes
>
>Keith

Ends previous posts.

Andreas, first, it's now clear that your comment on the two stage 
process refers to the base-base two-stage process:
http://journeytoforever.org/biodiesel_aleks.html

I'd assumed you meant the acid-base process:
http://journeytoforever.org/biodiesel_aleksnew.html

Anyway, I hope the processors bit is cleared up now - I'm not at all 
against continuous processors, but I won't agree that they're more 
suitable or that batch processors can't do the job.

>So - let's
>try it again (and apologies already now for the lengthy email that's to
>come:
>

Re: [biofuel] continuous process plans

2003-08-18 Thread Keith Addison

>Andrew,
>
>it seems I cannot attach anything to my emails. Would you like to give me
>your email-address that I can send you the patent as a tif-file?

The list doesn't accept attachments, as an essential anti-virus 
measure. Please contact me off-list about this, I can probably 
arrange something suitable.

Best wishes

Keith

>Dr. Andreas Ohnsorge




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Re: [biofuel] continuous process plans

2003-08-18 Thread J Allen

Guy you can go through a company call micro motion they make pump and 
meters that once are set they will deliver the amount you want and need. 
Jim Allen

Andreas W Ohnsorge wrote:

>
> Alan,
>
> interesting ideas - I am intending to use a used magnetic driven measuring
> pump (I found a couple of them in ebay) without the nonreturn valve in it.
> Usually they cost around 50 - 100 Euros (= Dollars?) in Germany. With the
> membrane they work like a piston driven oscillator. You can feed the
> reactor with another measuring pump that works in the normal way and is
> installed in line with the oscillator...
>
> What do you think?
>
> Andreas Ohnsorge
>
> CSC Ploenzke AG
> Abraham-Lincoln-Park 1
> 65189 Wiesbaden
> Germany
> Phone: +49.611.142.20020
> Fax: +49.611.142.980028
> Mobile:+49 172 - 8 43 30 32
> e-Mail: [EMAIL PROTECTED]
> Internet: http://www.de.csc.com
>
> 100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
> in der Team-Gesamtwertung http://www.csc-cycling.com/.
>
>
> 
>
> This is a PRIVATE message. If you are not the intended recipient, please
> delete without copying and kindly advise us by e-mail of the mistake in
> delivery. NOTE: Regardless of content, this e-mail shall not operate to
> bind CSC to any order or other contract unless pursuant to explicit 
> written
> agreement or government initiative expressly permitting the use of e-mail
> for such purpose.
> 
>
>
>
>
>   
>  
>
>   Alan 
> Petrillo  
>   
>
>biofuel@yahoogroups.com   
>  
>
>   @baylink.com>        
> cc:           
>   
>
>Subject: Re: [biofuel] 
> continuous process plans
>   18.08.2003 
> 09:18 
> 
>
>   Please 
> respond   
> 
>
>   to 
> biofuel   
> 
>
>   
>  
>
>   
>  
>
>
>
>
>
> Andreas W Ohnsorge wrote:
> >
> >Keith wrote:
> > FYI, there's a continuous reactor design here:
> > http://journeytoforever.org/biodiesel_processor.html#continuous
> >
> > Some people we know are working successfully with small-scale
> > continuous designs but they're not ready to talk about it yet.
> > Judging by their track record I'd be confident that they'll deliver
> > the goods in good order in due course. I know there's also been much
> > ado about continuous reactors at another forum, FWIW, but I haven't
> > taken any notice, not very interested.
>
> The OFM guys built their mixers, IMO, upside down with the pistons on
> the bottom and the pipes on top.
>
> When I designed the still partially built continuous processor that is
> sitting in boxes in my garage until I get to it again, I designed my
> OFMs with the pipes down in a heated water bath and the pistons on top.
>   Building the baffle assemblies for the pipes has proven to be one of
> the exciting parts.  Even more exciting has been building the pistons
> and oscilatory drives.  I'm trying to find access to a machine shop that
> won't cost me an arm and both legs to see what I can fabricate.  Unless
> I get some better ideas first.
>
> Now that it looks like I may actually need the thing I might actually
> finish building it.
>
>
> AP
>
>
>
> Biofuel at Journey to Forever:
> http://journeytoforever.org/biofuel.html
>
> Biofuels list archives:
> http://archive.nnytech.net/
>
> Please do NOT send Unsubscribe messages to the list 

Re: [biofuel] continuous process plans

2003-08-18 Thread Andreas W Ohnsorge


Alan,

interesting ideas - I am intending to use a used magnetic driven measuring
pump (I found a couple of them in ebay) without the nonreturn valve in it.
Usually they cost around 50 - 100 Euros (= Dollars?) in Germany. With the
membrane they work like a piston driven oscillator. You can feed the
reactor with another measuring pump that works in the normal way and is
installed in line with the oscillator...

What do you think?

Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
delete without copying and kindly advise us by e-mail of the mistake in
delivery. NOTE: Regardless of content, this e-mail shall not operate to
bind CSC to any order or other contract unless pursuant to explicit written
agreement or government initiative expressly permitting the use of e-mail
for such purpose.






   
  Alan Petrillo 
   
  cc:  
   
   Subject: Re: [biofuel] 
continuous process plans 
  18.08.2003 09:18  
   
  Please respond
   
  to biofuel
   

   

   




Andreas W Ohnsorge wrote:
>
 >Keith wrote:
> FYI, there's a continuous reactor design here:
> http://journeytoforever.org/biodiesel_processor.html#continuous
>
> Some people we know are working successfully with small-scale
> continuous designs but they're not ready to talk about it yet.
> Judging by their track record I'd be confident that they'll deliver
> the goods in good order in due course. I know there's also been much
> ado about continuous reactors at another forum, FWIW, but I haven't
> taken any notice, not very interested.

The OFM guys built their mixers, IMO, upside down with the pistons on
the bottom and the pipes on top.

When I designed the still partially built continuous processor that is
sitting in boxes in my garage until I get to it again, I designed my
OFMs with the pipes down in a heated water bath and the pistons on top.
  Building the baffle assemblies for the pipes has proven to be one of
the exciting parts.  Even more exciting has been building the pistons
and oscilatory drives.  I'm trying to find access to a machine shop that
won't cost me an arm and both legs to see what I can fabricate.  Unless
I get some better ideas first.

Now that it looks like I may actually need the thing I might actually
finish building it.


AP



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Re: [biofuel] continuous process plans

2003-08-18 Thread Alan Petrillo

Andreas W Ohnsorge wrote:
> 
 >Keith wrote:
> FYI, there's a continuous reactor design here:
> http://journeytoforever.org/biodiesel_processor.html#continuous
> 
> Some people we know are working successfully with small-scale
> continuous designs but they're not ready to talk about it yet.
> Judging by their track record I'd be confident that they'll deliver
> the goods in good order in due course. I know there's also been much
> ado about continuous reactors at another forum, FWIW, but I haven't
> taken any notice, not very interested.

The OFM guys built their mixers, IMO, upside down with the pistons on 
the bottom and the pipes on top.

When I designed the still partially built continuous processor that is 
sitting in boxes in my garage until I get to it again, I designed my 
OFMs with the pipes down in a heated water bath and the pistons on top. 
  Building the baffle assemblies for the pipes has proven to be one of 
the exciting parts.  Even more exciting has been building the pistons 
and oscilatory drives.  I'm trying to find access to a machine shop that 
won't cost me an arm and both legs to see what I can fabricate.  Unless 
I get some better ideas first.

Now that it looks like I may actually need the thing I might actually 
finish building it.


AP


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Re: [biofuel] continuous process plans

2003-08-17 Thread Andreas W Ohnsorge


Andrew,

it seems I cannot attach anything to my emails. Would you like to give me
your email-address that I can send you the patent as a tif-file?





Dr. Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
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  Andrew Lowe  To:  biofuel@yahoogroups.com 
   
   cc:  
   
  17.08.2003 08:22 Subject: Re: [biofuel] 
continuous process plans 
  Please respond
   
  to biofuel
   

   

   




Andreas W Ohnsorge wrote:
> Tomas,
>
> I am currently on some similar route - I had some experience with batch
> process and am about to construct a continuous processor following a
Patent
> from Metallgesellschaft out of 1985. Could explain a bit the basis of
your

 Could we please have some more info on this patent? Is it
German/US/British/Japanese/??? and do you have a number?

 Regards,
 Andrew

[SNIP]



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Re: [biofuel] continuous process plans

2003-08-17 Thread Andreas W Ohnsorge



Andrew,

the tif-file of the patent is here:

(See attached file: Patent-MG.tif)

If you need some explanations please let me know (it is in German...)



Dr. Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
delete without copying and kindly advise us by e-mail of the mistake in
delivery. NOTE: Regardless of content, this e-mail shall not operate to
bind CSC to any order or other contract unless pursuant to explicit written
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for such purpose.






   
  Andrew Lowe  To:  biofuel@yahoogroups.com 
   
   cc:  
   
  17.08.2003 08:22 Subject: Re: [biofuel] 
continuous process plans 
  Please respond
   
  to biofuel
   

   

   




Andreas W Ohnsorge wrote:
> Tomas,
>
> I am currently on some similar route - I had some experience with batch
> process and am about to construct a continuous processor following a
Patent
> from Metallgesellschaft out of 1985. Could explain a bit the basis of
your

 Could we please have some more info on this patent? Is it
German/US/British/Japanese/??? and do you have a number?

 Regards,
 Andrew

[SNIP]



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


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Re: [biofuel] continuous process plans

2003-08-17 Thread Andreas W Ohnsorge
ood for beeing used in equilibrium state reactions (like
>assumed here) - it should be preferred for quick reactions that easily
>reach the 100% end.
>
>Taking this into account the better reactor type for our biodiesel rection
>would be the pipe. Does anyone have any experience in using a pipe-type
>reactor for producing biodiesel? I think it could easily be built using
>plastic waste water pipes filles with glas or other inert media and mixed
>with pulse-pumps (membrane type for example). It would also have the
>advantage of continuous production
>
>Any thoughts about this approach?
>
>
>
>Andreas Ohnsorge


Hello Andreas

I think this is the wrong way round:

>... (first stage
>mass conversion to biodiesel and second stage the -more or less - 100%
>completion of that conversion).

It's in the second stage that there's mass conversion to biodiesel.
Of course 100% completion is not ever achieved. The goal is to arrive
within the limitations set by the various international standards,
and the processes available to us now are proven to be more than
capable of achieving that.

I think your conclusions about different types of reactors might
apply in laboratory conditions where accurate research results are
important, or in industry at large scale perhaps, but for homebrewers
and small-scale local producers at least, and probably well beyond
that, there isn't any need: the  batch-type stirred and heated
processors now in wide use are cheap, simple and effective.

FYI, there's a continuous reactor design here:
http://journeytoforever.org/biodiesel_processor.html#continuous

Some people we know are working successfully with small-scale
continuous designs but they're not ready to talk about it yet.
Judging by their track record I'd be confident that they'll deliver
the goods in good order in due course. I know there's also been much
ado about continuous reactors at another forum, FWIW, but I haven't
taken any notice, not very interested.

Best wishes

Keith



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Dr. Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
delete without copying and kindly advise us by e-mail of the mistake in
delivery. NOTE: Regardless of content, this e-mail shall not operate to
bind CSC to any order or other contract unless pursuant to explicit written
agreement or government initiative expressly permitting the use of e-mail
for such purpose.






   
  Keith Addison                 
   
 Subject: Re: [biofuel] 
continuous process plans 

   
  15.08.2003 23:19  
   
  Please respond
   
  to biofuel
   

   

   




Hello Andreas, Tomas and all

>Tomas,
>
>I am currently on some similar route - I had some experience with batch
>process and am about to construct a continuous processor following a
Patent
>from Metallgesellschaft out of 1985. Could explain a bit the basis of your
>process / could you give me your email address I really would like to get
>in contact with you and discuss the approaches...
>
>How do you think

Re: [biofuel] continuous process plans

2003-08-17 Thread Andrew Lowe

Andreas W Ohnsorge wrote:
> Tomas,
> 
> I am currently on some similar route - I had some experience with batch
> process and am about to construct a continuous processor following a Patent
> from Metallgesellschaft out of 1985. Could explain a bit the basis of your

Could we please have some more info on this patent? Is it 
German/US/British/Japanese/??? and do you have a number?

Regards,
Andrew

[SNIP]


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Re: [biofuel] continuous process plans

2003-08-15 Thread Keith Addison

Hello Andreas, Tomas and all

>Tomas,
>
>I am currently on some similar route - I had some experience with batch
>process and am about to construct a continuous processor following a Patent
>from Metallgesellschaft out of 1985. Could explain a bit the basis of your
>process / could you give me your email address I really would like to get
>in contact with you and discuss the approaches...
>
>How do you think?

I think it would be much better if you discussed it on-list instead 
of privately, so that everyone could share in and hopefully 
contribute to the discussion.

Best wishes

Keith Addison
Journey to Forever

>
>Andreas Ohnsorge
>
>CSC Ploenzke AG
>Abraham-Lincoln-Park 1
>65189 Wiesbaden
>Germany
>Phone: +49.611.142.20020
>Fax: +49.611.142.980028
>Mobile:+49 172 - 8 43 30 32
>e-Mail: [EMAIL PROTECTED]
>Internet: http://www.de.csc.com
>
>100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
>in der Team-Gesamtwertung http://www.csc-cycling.com/.
>
>
>- 
>---
>
>This is a PRIVATE message. If you are not the intended recipient, please
>delete without copying and kindly advise us by e-mail of the mistake in
>delivery. NOTE: Regardless of content, this e-mail shall not operate to
>bind CSC to any order or other contract unless pursuant to explicit written
>agreement or government initiative expressly permitting the use of e-mail
>for such purpose.
>- 
>---
>
>
>
>
> 
>
>  Johnsson Tomas 
>
>  "'biofuel@yahoogroups.com'"  
>
>  @pohjola.fi> cc: 
>
>   Subject: [biofuel] 
>continuous process plans
>  15.08.2003 09:10 
>
>  Please respond 
>
>  to biofuel 
>
> 
>
> 
>
>
>
>
>
>Hello All,
>
>During long nights of batch processing BD the idea of building a continuous
>process has been born. The first ideas is to make a standing
>oscilatorprocessor. The feeding of the catalyt and the oil we are planning
>to do with hose pumps. The pumps by it self has a 1% accuracy and by
>keeping
>the oil at same temperature before feeding it through the pump the accuracy
>could be kept close to the 1%.
>
>Do some one have experince from contiuouse process making of BD and can
>tell
>about their experince from the system and making BD this way.
>
>The hardware side at this moment seams to be solved and can proceed
>according to the idea and start to plan the building meanwhile there is
>still a ton of basic questions about the chemical reaction open which can
>turn the hardware side upside down. The methanol amount we have a idea of
>keeping close to 22 % of the oil amount but If we have a accuracy of 1% by
>the pumps this means that for a oil using 6 gram/lye/liter the amount could
>come close to 6.1 gram/lye/litre or 5.9 gram/lye/litre continuously.
>According to our experince this will be close to what can be tolerated.
>Will
>the 1 % accuracy be enought.
>
>Any opinions, thoughts or comments?
>
>The autum is slovely on the way, light wind, clear sky, +18 ¡C in IngŒ,
>Finland.
>Regards
>Tomas


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Re: [biofuel] continuous process plans

2003-08-15 Thread Andreas W Ohnsorge


Tomas,

I am currently on some similar route - I had some experience with batch
process and am about to construct a continuous processor following a Patent
from Metallgesellschaft out of 1985. Could explain a bit the basis of your
process / could you give me your email address I really would like to get
in contact with you and discuss the approaches...

How do you think?


Andreas Ohnsorge

CSC Ploenzke AG
Abraham-Lincoln-Park 1
65189 Wiesbaden
Germany
Phone: +49.611.142.20020
Fax: +49.611.142.980028
Mobile:+49 172 - 8 43 30 32
e-Mail: [EMAIL PROTECTED]
Internet: http://www.de.csc.com

100 Jahre Tour de France: Herzlichen GlŸckwunsch dem Team CSC zum 1. Platz
in der Team-Gesamtwertung http://www.csc-cycling.com/.




This is a PRIVATE message. If you are not the intended recipient, please
delete without copying and kindly advise us by e-mail of the mistake in
delivery. NOTE: Regardless of content, this e-mail shall not operate to
bind CSC to any order or other contract unless pursuant to explicit written
agreement or government initiative expressly permitting the use of e-mail
for such purpose.






   
  Johnsson Tomas
   

  @pohjola.fi> cc:  
   
   Subject: [biofuel] continuous 
process plans 
  15.08.2003 09:10  
   
  Please respond
   
  to biofuel
   

   

   




Hello All,

During long nights of batch processing BD the idea of building a continuous
process has been born. The first ideas is to make a standing
oscilatorprocessor. The feeding of the catalyt and the oil we are planning
to do with hose pumps. The pumps by it self has a 1% accuracy and by
keeping
the oil at same temperature before feeding it through the pump the accuracy
could be kept close to the 1%.

Do some one have experince from contiuouse process making of BD and can
tell
about their experince from the system and making BD this way.

The hardware side at this moment seams to be solved and can proceed
according to the idea and start to plan the building meanwhile there is
still a ton of basic questions about the chemical reaction open which can
turn the hardware side upside down. The methanol amount we have a idea of
keeping close to 22 % of the oil amount but If we have a accuracy of 1% by
the pumps this means that for a oil using 6 gram/lye/liter the amount could
come close to 6.1 gram/lye/litre or 5.9 gram/lye/litre continuously.
According to our experince this will be close to what can be tolerated.
Will
the 1 % accuracy be enought.

Any opinions, thoughts or comments?

The autum is slovely on the way, light wind, clear sky, +18 ¡C in IngŒ,
Finland.
Regards
Tomas


Biofuel at Journey to Forever:
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