Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-18 Thread Keith Addison

Hello Mark, Tomas and all

>Tomas,
>
>Where could I buy one at this price?
>
>I centrifuge all materials before washing on a
>lab level, so using the Alfie unit would give a
>level of automation.
>
>One problem you are having is residual glycerol
>contamination in the wash water causing it to
>cloud very quickly.

Yes, as already pointed out. Not settling for long enough before the 
wash, or not washing enough.

>I find separating the two
>phases (ME and Glycerol) first such that they are
>both clear allows for a far cleaner wash.
>Further, I also find neutralising the pH wash
>water allows for a long term clear final product.
>Phosphoric acid will on a very small volume level
>crack the soaps back to FFA.
>
>I have two trains of thought on this -
>
>1) I use ~10% by volume wash water pH neutralised
>on a automated closed loop system. It needs to be
>washed only once and the amount of H3PO4 used is
>in relative terms quite small. The wash water
>clears and hence can be recycled time and time
>again. But remember the soap will return back to
>FFA. The pysical volume with respect to the final
>bio-diesel is very small indeed, maybe 0.001%
>v/v.

How did you calculate that? If it's that small an amount of FFA, then 
that little soap wouldn't make that much difference in washing, seems 
to me.

>2) Wash the biodiesel with tap water say 2 or 3
>times until the final stage water is clear. Spent
>water has to be put down the drain, which is a
>waste.

No it doesn't, and no it isn't. You should reuse it - use the 2nd 
wash water for the next batch first wash, the 3rd wash water for the 
next batch 2nd wash and so on. So you're using each wash three times, 
only the 3rd wash is fresh. The first wash can't be reused, but it 
doesn't have to go down the drain either. A simple grey-water system 
will handle it well. We currently feed it to water hyacinths and 
duckweed, and compost the plants. Next step will be to reclaim 
cleansed water from the water hycinths and duckweed.

>In either case, the final glycerol can be pH
>neutralised with H3PO4 under closed loop control,
>the Sodium Phosphate precipitate removed via
>centrifuge, the water and ME separated via
>centrifuge. The final product is clear ME,
>neutral Glycerol and a compact solid fertilizer
>base.

If you believe in "fertilizers". Even if you do, mopst phosphates are 
applied to phosphate-rich soil, and most of what's applied quickly 
becomes unavailable to plants, like the rest. Phosphates are made 
available by biological action via the soil micro-life. Keep the 
micro-life happy and you don't need phosphates, nor any other 
"fertilizers".

Anyway, what do you mean by "neutral Glycerol"? You've accounted for 
the catalyst in the by-product cocktail, but not for the soap/FFA, 
which is probably most of it, and not for the excess methanol.

I don't understand the perceived need for centrifuges etc etc etc. 
What for? It increases the production rate? I don't think so - maybe 
it shortens the production *time*. Well, so what? Settling, washing, 
bubble-drying will take maybe 4-5 days from starting processing to 
finished, clear fuel. So if you have space to store 4-5 days' 
production, that's all you need. If you've got your processing right, 
that is - if you find a need for all this just for a "cleaner wash" 
it might help to pay some attention to optimizing your process. 
Whatever, what I've seen of centrifuges so far doesn't exactly 
impress, and nor does the price.

Best

Keith


>Mark
>
>=
>Mark Schofield
>M.Sc B.Eng DHE AMIMechE
>t 07944 401662
>e [EMAIL PROTECTED]
>Autogas Conversions and LPG Pumps


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RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-23 Thread Keith Addison

Hello Peter

>Keith,
>I use to represent ALFA LAVAL as a local agent here in Tanzania. They
>provide centrifugal separation units for a wide range of raw materials,
>I was dealing in the Powergen side and units are used for cleaning lube
>and fuel oil in power generation. Then can be set-up to remove several
>phases which would prove very efficient on a large scale fuel
>clean-up/washing situation.
>
>Have a look at www/alfalaval.com
>They also deal in used equipment (factory reconditioned)

Thankyou, but I have no interest in centrifuges - as my message below says:

>I don't understand the perceived need for centrifuges etc etc etc.
>What for? It increases the production rate? I don't think so - maybe
>it shortens the production *time*. Well, so what? Settling, washing,
>bubble-drying will take maybe 4-5 days from starting processing to
>finished, clear fuel. So if you have space to store 4-5 days'
>production, that's all you need. If you've got your processing right,
>that is - if you find a need for all this just for a "cleaner wash"
>it might help to pay some attention to optimizing your process.
>Whatever, what I've seen of centrifuges so far doesn't exactly
>impress, and nor does the price.

Not interested in large-scale operations either. But others here are.

Thanks anyway.

Keith Addison
Journey to Forever


>Peter
>
>-Original Message-
>From: Keith Addison [mailto:[EMAIL PROTECTED]
>Sent: Thursday, September 18, 2003 9:57 AM
>To: biofuel@yahoogroups.com
>Cc: biofuels-biz@yahoogroups.com
>Subject: Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME
>
>Hello Mark, Tomas and all
>
> >Tomas,
> >
> >Where could I buy one at this price?
> >
> >I centrifuge all materials before washing on a
> >lab level, so using the Alfie unit would give a
> >level of automation.
> >
> >One problem you are having is residual glycerol
> >contamination in the wash water causing it to
> >cloud very quickly.
>
>Yes, as already pointed out. Not settling for long enough before the
>wash, or not washing enough.
>
> >I find separating the two
> >phases (ME and Glycerol) first such that they are
> >both clear allows for a far cleaner wash.
> >Further, I also find neutralising the pH wash
> >water allows for a long term clear final product.
> >Phosphoric acid will on a very small volume level
> >crack the soaps back to FFA.
> >
> >I have two trains of thought on this -
> >
> >1) I use ~10% by volume wash water pH neutralised
> >on a automated closed loop system. It needs to be
> >washed only once and the amount of H3PO4 used is
> >in relative terms quite small. The wash water
> >clears and hence can be recycled time and time
> >again. But remember the soap will return back to
> >FFA. The pysical volume with respect to the final
> >bio-diesel is very small indeed, maybe 0.001%
> >v/v.
>
>How did you calculate that? If it's that small an amount of FFA, then
>that little soap wouldn't make that much difference in washing, seems
>to me.
>
> >2) Wash the biodiesel with tap water say 2 or 3
> >times until the final stage water is clear. Spent
> >water has to be put down the drain, which is a
> >waste.
>
>No it doesn't, and no it isn't. You should reuse it - use the 2nd
>wash water for the next batch first wash, the 3rd wash water for the
>next batch 2nd wash and so on. So you're using each wash three times,
>only the 3rd wash is fresh. The first wash can't be reused, but it
>doesn't have to go down the drain either. A simple grey-water system
>will handle it well. We currently feed it to water hyacinths and
>duckweed, and compost the plants. Next step will be to reclaim
>cleansed water from the water hycinths and duckweed.
>
> >In either case, the final glycerol can be pH
> >neutralised with H3PO4 under closed loop control,
> >the Sodium Phosphate precipitate removed via
> >centrifuge, the water and ME separated via
> >centrifuge. The final product is clear ME,
> >neutral Glycerol and a compact solid fertilizer
> >base.
>
>If you believe in "fertilizers". Even if you do, mopst phosphates are
>applied to phosphate-rich soil, and most of what's applied quickly
>becomes unavailable to plants, like the rest. Phosphates are made
>available by biological action via the soil micro-life. Keep the
>micro-life happy and you don't need phosphates, nor any other
>"fertilizers".
>
>Anyway, what do you mean by "neutral Glycerol"? You've accounted for
>the catalyst in the by-product coc

RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-23 Thread mark schofield

Keith

I feel centrifuges are the future of mass
production. Our plant has a production capability
of 700,000L per week so I cant avoid using them.

ark


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RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-23 Thread Keith Addison

>Keith
>
>I feel centrifuges are the future of mass
>production. Our plant has a production capability
>of 700,000L per week so I cant avoid using them.
>
>ark

No doubt, but the focus of this group, and our focus at Journey to 
Forever, is not on mass production and large production-capacity 
plants but on small-scale, decentralized, localized production, and 
in this setting I see no need for nor advantage in centrifuges. As 
previously explained.

Meanwhile I asked you a couple of questions in the message below, but 
got no response from you.

Keith


>Hello Mark, Tomas and all
>
>>Tomas,
>>
>>Where could I buy one at this price?
>>
>>I centrifuge all materials before washing on a
>>lab level, so using the Alfie unit would give a
>>level of automation.
>>
>>One problem you are having is residual glycerol
>>contamination in the wash water causing it to
>>cloud very quickly.
>
>Yes, as already pointed out. Not settling for long enough before the 
>wash, or not washing enough.
>
>>I find separating the two
>>phases (ME and Glycerol) first such that they are
>>both clear allows for a far cleaner wash.
>>Further, I also find neutralising the pH wash
>>water allows for a long term clear final product.
>>Phosphoric acid will on a very small volume level
>>crack the soaps back to FFA.
>>
>>I have two trains of thought on this -
>>
>>1) I use ~10% by volume wash water pH neutralised
>>on a automated closed loop system. It needs to be
>>washed only once and the amount of H3PO4 used is
>>in relative terms quite small. The wash water
>>clears and hence can be recycled time and time
>>again. But remember the soap will return back to
>>FFA. The pysical volume with respect to the final
>>bio-diesel is very small indeed, maybe 0.001%
>>v/v.
>
>How did you calculate that? If it's that small an amount of FFA, 
>then that little soap wouldn't make that much difference in washing, 
>seems to me.
>
>>2) Wash the biodiesel with tap water say 2 or 3
>>times until the final stage water is clear. Spent
>>water has to be put down the drain, which is a
>>waste.
>
>No it doesn't, and no it isn't. You should reuse it - use the 2nd 
>wash water for the next batch first wash, the 3rd wash water for the 
>next batch 2nd wash and so on. So you're using each wash three 
>times, only the 3rd wash is fresh. The first wash can't be reused, 
>but it doesn't have to go down the drain either. A simple grey-water 
>system will handle it well. We currently feed it to water hyacinths 
>and duckweed, and compost the plants. Next step will be to reclaim 
>cleansed water from the water hyacinths and duckweed.
>
>>In either case, the final glycerol can be pH
>>neutralised with H3PO4 under closed loop control,
>>the Sodium Phosphate precipitate removed via
>>centrifuge, the water and ME separated via
>>centrifuge. The final product is clear ME,
>>neutral Glycerol and a compact solid fertilizer
>>base.
>
>If you believe in "fertilizers". Even if you do, most phosphates are 
>applied to phosphate-rich soil, and most of what's applied quickly 
>becomes unavailable to plants, like the rest. Phosphates are made 
>available by biological action via the soil micro-life. Keep the 
>micro-life happy and you don't need phosphates, nor any other 
>"fertilizers".
>
>Anyway, what do you mean by "neutral Glycerol"? You've accounted for 
>the catalyst in the by-product cocktail, but not for the soap/FFA, 
>which is probably most of it, and not for the excess methanol.
>
>I don't understand the perceived need for centrifuges etc etc etc. 
>What for? It increases the production rate? I don't think so - maybe 
>it shortens the production *time*. Well, so what? Settling, washing, 
>bubble-drying will take maybe 4-5 days from starting processing to 
>finished, clear fuel. So if you have space to store 4-5 days' 
>production, that's all you need. If you've got your processing 
>right, that is - if you find a need for all this just for a "cleaner 
>wash" it might help to pay some attention to optimizing your 
>process. Whatever, what I've seen of centrifuges so far doesn't 
>exactly impress, and nor does the price.
>
>Best
>
>Keith
>
>
>>Mark
>>
>>=
>>Mark Schofield
>>M.Sc B.Eng DHE AMIMechE
>>t 07944 401662
>>e [EMAIL PROTECTED]
>>Autogas Conversions and LPG Pumps


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Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-23 Thread Appal Energy

Yes Mark.

But have you conducted a cost benefit analysis that includes all
externalities, or simply "profit/loss?"

As a general rule, unless of course you're sitting in the middle of a
plethora of palm plantations all within spitting distance of each other,
macro production incurs greater consumption of inumerable resources than
does micro- and bio-regional production, all-the-while draining capital,
resources and jobs from smaller communities.

Not exactly a model for "sharing the wealth."

Todd Swearingen


- Original Message - 
From: "mark schofield" <[EMAIL PROTECTED]>
To: 
Sent: Tuesday, September 23, 2003 12:15 PM
Subject: RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME


> Keith
>
> I feel centrifuges are the future of mass
> production. Our plant has a production capability
> of 700,000L per week so I cant avoid using them.
>
> ark
>
> 
> Want to chat instantly with your online friends?  Get the FREE Yahoo!
> Messenger http://mail.messenger.yahoo.co.uk
>
>
>
> 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] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-23 Thread Peter

Keith,
I use to represent ALFA LAVAL as a local agent here in Tanzania. They
provide centrifugal separation units for a wide range of raw materials,
I was dealing in the Powergen side and units are used for cleaning lube
and fuel oil in power generation. Then can be set-up to remove several
phases which would prove very efficient on a large scale fuel
clean-up/washing situation.
 
Have a look at www/alfalaval.com
They also deal in used equipment (factory reconditioned)
 
 
 
Peter 
 
-Original Message-
From: Keith Addison [mailto:[EMAIL PROTECTED] 
Sent: Thursday, September 18, 2003 9:57 AM
To: biofuel@yahoogroups.com
Cc: biofuels-biz@yahoogroups.com
Subject: Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME
 
Hello Mark, Tomas and all

>Tomas,
>
>Where could I buy one at this price?
>
>I centrifuge all materials before washing on a
>lab level, so using the Alfie unit would give a
>level of automation.
>
>One problem you are having is residual glycerol
>contamination in the wash water causing it to
>cloud very quickly.

Yes, as already pointed out. Not settling for long enough before the 
wash, or not washing enough.

>I find separating the two
>phases (ME and Glycerol) first such that they are
>both clear allows for a far cleaner wash.
>Further, I also find neutralising the pH wash
>water allows for a long term clear final product.
>Phosphoric acid will on a very small volume level
>crack the soaps back to FFA.
>
>I have two trains of thought on this -
>
>1) I use ~10% by volume wash water pH neutralised
>on a automated closed loop system. It needs to be
>washed only once and the amount of H3PO4 used is
>in relative terms quite small. The wash water
>clears and hence can be recycled time and time
>again. But remember the soap will return back to
>FFA. The pysical volume with respect to the final
>bio-diesel is very small indeed, maybe 0.001%
>v/v.

How did you calculate that? If it's that small an amount of FFA, then 
that little soap wouldn't make that much difference in washing, seems 
to me.

>2) Wash the biodiesel with tap water say 2 or 3
>times until the final stage water is clear. Spent
>water has to be put down the drain, which is a
>waste.

No it doesn't, and no it isn't. You should reuse it - use the 2nd 
wash water for the next batch first wash, the 3rd wash water for the 
next batch 2nd wash and so on. So you're using each wash three times, 
only the 3rd wash is fresh. The first wash can't be reused, but it 
doesn't have to go down the drain either. A simple grey-water system 
will handle it well. We currently feed it to water hyacinths and 
duckweed, and compost the plants. Next step will be to reclaim 
cleansed water from the water hycinths and duckweed.

>In either case, the final glycerol can be pH
>neutralised with H3PO4 under closed loop control,
>the Sodium Phosphate precipitate removed via
>centrifuge, the water and ME separated via
>centrifuge. The final product is clear ME,
>neutral Glycerol and a compact solid fertilizer
>base.

If you believe in "fertilizers". Even if you do, mopst phosphates are 
applied to phosphate-rich soil, and most of what's applied quickly 
becomes unavailable to plants, like the rest. Phosphates are made 
available by biological action via the soil micro-life. Keep the 
micro-life happy and you don't need phosphates, nor any other 
"fertilizers".

Anyway, what do you mean by "neutral Glycerol"? You've accounted for 
the catalyst in the by-product cocktail, but not for the soap/FFA, 
which is probably most of it, and not for the excess methanol.

I don't understand the perceived need for centrifuges etc etc etc. 
What for? It increases the production rate? I don't think so - maybe 
it shortens the production *time*. Well, so what? Settling, washing, 
bubble-drying will take maybe 4-5 days from starting processing to 
finished, clear fuel. So if you have space to store 4-5 days' 
production, that's all you need. If you've got your processing right, 
that is - if you find a need for all this just for a "cleaner wash" 
it might help to pay some attention to optimizing your process. 
Whatever, what I've seen of centrifuges so far doesn't exactly 
impress, and nor does the price.

Best

Keith


>Mark
>
>=
>Mark Schofield
>M.Sc B.Eng DHE AMIMechE
>t 07944 401662
>e [EMAIL PROTECTED]
>Autogas Conversions and LPG Pumps





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Bi

RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-26 Thread mark schofield

Keith

OK, soap cracks back to FFA with H3PO4 hence
keeping the water clear. FFA volume is quite
small. Just on my way out hence short reply.

Mark

 --- Keith Addison <[EMAIL PROTECTED]>
wrote: > >Keith
> >
> >I feel centrifuges are the future of mass
> >production. Our plant has a production
> capability
> >of 700,000L per week so I cant avoid using
> them.
> >
> >ark
> 
> No doubt, but the focus of this group, and our
> focus at Journey to 
> Forever, is not on mass production and large
> production-capacity 
> plants but on small-scale, decentralized,
> localized production, and 
> in this setting I see no need for nor advantage
> in centrifuges. As 
> previously explained.
> 
> Meanwhile I asked you a couple of questions in
> the message below, but 
> got no response from you.
> 
> Keith
> 
> 
> >Hello Mark, Tomas and all
> >
> >>Tomas,
> >>
> >>Where could I buy one at this price?
> >>
> >>I centrifuge all materials before washing on
> a
> >>lab level, so using the Alfie unit would give
> a
> >>level of automation.
> >>
> >>One problem you are having is residual
> glycerol
> >>contamination in the wash water causing it to
> >>cloud very quickly.
> >
> >Yes, as already pointed out. Not settling for
> long enough before the 
> >wash, or not washing enough.
> >
> >>I find separating the two
> >>phases (ME and Glycerol) first such that they
> are
> >>both clear allows for a far cleaner wash.
> >>Further, I also find neutralising the pH wash
> >>water allows for a long term clear final
> product.
> >>Phosphoric acid will on a very small volume
> level
> >>crack the soaps back to FFA.
> >>
> >>I have two trains of thought on this -
> >>
> >>1) I use ~10% by volume wash water pH
> neutralised
> >>on a automated closed loop system. It needs
> to be
> >>washed only once and the amount of H3PO4 used
> is
> >>in relative terms quite small. The wash water
> >>clears and hence can be recycled time and
> time
> >>again. But remember the soap will return back
> to
> >>FFA. The pysical volume with respect to the
> final
> >>bio-diesel is very small indeed, maybe 0.001%
> >>v/v.
> >
> >How did you calculate that? If it's that small
> an amount of FFA, 
> >then that little soap wouldn't make that much
> difference in washing, 
> >seems to me.
> >
> >>2) Wash the biodiesel with tap water say 2 or
> 3
> >>times until the final stage water is clear.
> Spent
> >>water has to be put down the drain, which is
> a
> >>waste.
> >
> >No it doesn't, and no it isn't. You should
> reuse it - use the 2nd 
> >wash water for the next batch first wash, the
> 3rd wash water for the 
> >next batch 2nd wash and so on. So you're using
> each wash three 
> >times, only the 3rd wash is fresh. The first
> wash can't be reused, 
> >but it doesn't have to go down the drain
> either. A simple grey-water 
> >system will handle it well. We currently feed
> it to water hyacinths 
> >and duckweed, and compost the plants. Next
> step will be to reclaim 
> >cleansed water from the water hyacinths and
> duckweed.
> >
> >>In either case, the final glycerol can be pH
> >>neutralised with H3PO4 under closed loop
> control,
> >>the Sodium Phosphate precipitate removed via
> >>centrifuge, the water and ME separated via
> >>centrifuge. The final product is clear ME,
> >>neutral Glycerol and a compact solid
> fertilizer
> >>base.
> >
> >If you believe in "fertilizers". Even if you
> do, most phosphates are 
> >applied to phosphate-rich soil, and most of
> what's applied quickly 
> >becomes unavailable to plants, like the rest.
> Phosphates are made 
> >available by biological action via the soil
> micro-life. Keep the 
> >micro-life happy and you don't need
> phosphates, nor any other 
> >"fertilizers".
> >
> >Anyway, what do you mean by "neutral
> Glycerol"? You've accounted for 
> >the catalyst in the by-product cocktail, but
> not for the soap/FFA, 
> >which is probably most of it, and not for the
> excess methanol.
> >
> >I don't understand the perceived need for
> centrifuges etc etc etc. 
> >What for? It increases the production rate? I
> don't think so - maybe 
> >it shortens the production *time*. Well, so
> what? Settling, washing, 
> >bubble-drying will take maybe 4-5 days from
> starting processing to 
> >finished, clear fuel. So if you have space to
> store 4-5 days' 
> >production, that's all you need. If you've got
> your processing 
> >right, that is - if you find a need for all
> this just for a "cleaner 
> >wash" it might help to pay some attention to
> optimizing your 
> >process. Whatever, what I've seen of
> centrifuges so far doesn't 
> >exactly impress, and nor does the price.
> >
> >Best
> >
> >Keith
> >
> >
> >>Mark
> >>
> >>=
> >>Mark Schofield
> >>M.Sc B.Eng DHE AMIMechE
> >>t 07944 401662
> >>e [EMAIL PROTECTED]
> >>Autogas Conversions and LPG Pumps
> 
>  


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Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-26 Thread mark schofield

Todd,

Yes I have. We buy in contract amount of fat and
oil delivered to site via tanker. Remember that
the UK is a relatively small place peaking at
1000 miles long by 200 wide. 

Regards

Mark


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RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-26 Thread Keith Addison

>Keith
>
>OK, soap cracks back to FFA with H3PO4 hence
>keeping the water clear. FFA volume is quite
>small. Just on my way out hence short reply.
>
>Mark

I hope you'll send a more detailed one when you come back.

We all know acid cracks soap back to FFA, you already said that, 
twice, now three times:

> > >>Phosphoric acid will on a very small volume level
> > >>crack the soaps back to FFA.

And that wasn't the question. This was:

> > >>again. But remember the soap will return back
> > to
> > >>FFA. The pysical volume with respect to the
> > final
> > >>bio-diesel is very small indeed, maybe 0.001%
> > >>v/v.
> > >
> > >How did you calculate that? If it's that small
> > an amount of FFA,
> > >then that little soap wouldn't make that much
> > difference in washing,
> > >seems to me.

How did you calculate the 0.001% v/v? There are a lot of variables at 
play there, yet you give such a precise figure, what's it based on? 
This isn't very precise: "... the amount of H3PO4 used is in relative 
terms quite small" and "... a very small volume level".

There were other questions. You also said 2-3 washes with tapwater 
wastes the water, which isn't so, and you don't appear to have 
considered using 2-3 washes with acid added to the first wash, which 
many people do.

You also talked of "neutral Glycerol":

> > >>In either case, the final glycerol can be pH
> > >>neutralised with H3PO4 under closed loop
> > control,
> > >>the Sodium Phosphate precipitate removed via
> > >>centrifuge, the water and ME separated via
> > >>centrifuge. The final product is clear ME,
> > >>neutral Glycerol and a compact solid
> > fertilizer
> > >>base.
> > >
> > >Anyway, what do you mean by "neutral Glycerol"? You've accounted for
> > >the catalyst in the by-product cocktail, but not for the soap/FFA,
> > >which is probably most of it, and not for the excess methanol.

I'm not just asking for the sake of asking - surely you're aware that 
the pros and cons of acid-washing are a long-running controversy, it 
often comes up on the list, with some progress being made at last 
towards a resolution. You've posted this very low figure for the FFA 
quantities, which would certainly be relevant to the discussion, only 
you don't say what it's based on, it doesn't quite make sense, and it 
tends to ignore all the variables, not only the obvious ones but also 
the less obvious ones such as the different FA profiles of different 
oils, and how the different acids might behave in a wash, as pointed 
out recently by Prof. Michael Allen and cross-posted here. So please 
explain.

The whole message doesn't quite make sense, and seems rather odd for 
someone with a 700,000L per week biodiesel plant. Do you have such a 
plant? I mean up and running? A week or so ago you were talking of 
laboratory-level experiments, a couple of months back you were making 
your first test batches. You say there's a 700,000L per week 
biodiesel plant operating in the UK, that's nearly 10 million US 
gallons a year, which would surely make rather a large and loud dent 
in the market there even if it's operating at well below the 
production capability you claim, but we've heard nothing of it except 
from you.

Keith Addison
Journey to Forever


> --- Keith Addison <[EMAIL PROTECTED]>
>wrote: > >Keith
> > >
> > >I feel centrifuges are the future of mass
> > >production. Our plant has a production
> > capability
> > >of 700,000L per week so I cant avoid using
> > them.
> > >
> > >ark
> >
> > No doubt, but the focus of this group, and our
> > focus at Journey to
> > Forever, is not on mass production and large
> > production-capacity
> > plants but on small-scale, decentralized,
> > localized production, and
> > in this setting I see no need for nor advantage
> > in centrifuges. As
> > previously explained.
> >
> > Meanwhile I asked you a couple of questions in
> > the message below, but
> > got no response from you.
> >
> > Keith
> >
> >
> > >Hello Mark, Tomas and all
> > >
> > >>Tomas,
> > >>
> > >>Where could I buy one at this price?
> > >>
> > >>I centrifuge all materials before washing on
> > a
> > >>lab level, so using the Alfie unit would give
> > a
> > >>level of automation.
> > >>
> > >>One problem you are having is residual
> > glycerol
> > >>contamination in the wash water causing it to
> > >>cloud very quickly.
> > >
> > >Yes, as already pointed out. Not settling for
> > long enough before the
> > >wash, or not washing enough.
> > >
> > >>I find separating the two
> > >>phases (ME and Glycerol) first such that they
> > are
> > >>both clear allows for a far cleaner wash.
> > >>Further, I also find neutralising the pH wash
> > >>water allows for a long term clear final
> > product.
> > >>Phosphoric acid will on a very small volume
> > level
> > >>crack the soaps back to FFA.
> > >>
> > >>I have two trains of thought on this -
> > >>
> > >>1) I use ~10% by volume wash water pH
> > neutralised
> > >>on a automated closed loop system. It needs
> > to be
> > >>w

RE: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-10-01 Thread mark schofield

Dear Keith

OK, I'll expand a little. We are building a large
plant here in the UK with a production capacity
of 700,000L per week.

I have spent the last 3-5 months everyday except
Sunday (~1560 hrs total) experimenting and
perfecting as far as possible the single base
stage and the acid-base two stage. I have
produced very repeatable results. I can heat the
oil (60'C+) and allow to cool. It cools clear. I
can then freeze the oil allow to thaw and
centrifuge off the solid material (very small
quantity of longer esters) for a mildly
winterised fuel if I want to. The US Military
used exactly the same technique for their gas
turbine experiments. The UK standard for
Bio-diesel is EN 14214. I have a copy here is
anybody wants one.

Keith, I can only explain what I have achieved
though not all of this will be relevant to you in
terms of an automated process.

When I manufacture the methyl esters, all of the
glycerol is removed from the bio-diesel via
centrifuge either now in a lab or in 2-3 months
time in an Alfa Laval unit (7500L per hr). At
this stage the bio-diesel is clear and crisp. I
need only to add a very small quantity of water,
of order 10-20% and wash just once. The biodiesel
pH at this stage is 11. I took serious note of
you stating not to exceed 9-9.5 some weeks ago.
However, I specifically repeated the experiments
at pH 9.5 and the results were not as good as 11.
I am operating with a molar ratio of 4.89 : 1
methanol to oil. 

OK, at this stage I have clear bio-diesel free
from glycerol and FFA. The centrifuge operates at
3500rpm. The water and methanol are flash
evaporated in a thin film extraction unit. Once
the water is added the two liquids are either
bubble mixed in the lab or later will be pump
mixed on site in SS316 10,000L tanks. After a few
minutes, the phosphoric acid is introduced until
the pH of the whole batch reaches 7.00 +/- 0.1.
The solid sodium phosphate precipitates out very
fast and is removed in the lab via small
centrifuge and on site via self-cleaning
industrial Alfa Laval units. The finished product
is clean, clear and crisp. 

I have set aside the glycerol in a separate SS316
4500L tank, where all the excess water and
methanol are flash evaporated and the remaining
liquid neutralised. The sodium phosphate is
removed as before. The centrifuge also separates
the FFA into a third holding tank for continuous
esterification before trans-esterification.

So, when I said the FFA content at the wash stage
is very low it is of order 0.01% or less at a
guess since all of the residual FFA has been
removed in the centrifuge. The wash water stays
relatively clean even over 12 hr wash cycles. I
donât have any problems associated with needing
more than 1 wash etc. In terms of H3PO4
consumption, I use enough 85% to bring to pH to
7.00 +/- 0.1. Realistically Iâd use something
like 5cc per L off the top of my head. With
regard to the soap question you have proposed, I
simply neutralise and extract the glycerol,
sodium phosphate and FFA in a tuned 3-way
centrifuge for post processing. I have not
experimented with differing acids for the
neutralisation process i.e. HCl for NaCl
extraction etc. 

With regard to the plant, I didnât say anything
for the last few months. The money has only just
been put into place. This plant at 700,000L per
week isnât the largest here, though it is 2nd or
will be shortly. Ours is based into a 10,000
sq.ft building, which is being re-furbished
currently. I have worked on emissions and
alternative fuels since 1999. I had experimented
with bio-diesel then but didnât have time to
finish it, hence the fast up-take this time
around. Putting the process under automatic
control is far easier than manufacturing small
batches.

If I have made mistakes or points are not clear,
please ask.

I missed the conversation from Prof Allen ö has
this been stored in the archive?

Regards

Mark


=
Mark Schofield
M.Sc B.Eng DHE AMIMechE 
t 07944 401662 
e [EMAIL PROTECTED]
Autogas Conversions and LPG Pumps


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[biofuels-biz] Re: [biofuel] USING SEPARATOR FOR AFTER WASH TREATMENT OF ME

2003-09-18 Thread Keith Addison

Hello Mark, Tomas and all

>Tomas,
>
>Where could I buy one at this price?
>
>I centrifuge all materials before washing on a
>lab level, so using the Alfie unit would give a
>level of automation.
>
>One problem you are having is residual glycerol
>contamination in the wash water causing it to
>cloud very quickly.

Yes, as already pointed out. Not settling for long enough before the 
wash, or not washing enough.

>I find separating the two
>phases (ME and Glycerol) first such that they are
>both clear allows for a far cleaner wash.
>Further, I also find neutralising the pH wash
>water allows for a long term clear final product.
>Phosphoric acid will on a very small volume level
>crack the soaps back to FFA.
>
>I have two trains of thought on this -
>
>1) I use ~10% by volume wash water pH neutralised
>on a automated closed loop system. It needs to be
>washed only once and the amount of H3PO4 used is
>in relative terms quite small. The wash water
>clears and hence can be recycled time and time
>again. But remember the soap will return back to
>FFA. The pysical volume with respect to the final
>bio-diesel is very small indeed, maybe 0.001%
>v/v.

How did you calculate that? If it's that small an amount of FFA, then 
that little soap wouldn't make that much difference in washing, seems 
to me.

>2) Wash the biodiesel with tap water say 2 or 3
>times until the final stage water is clear. Spent
>water has to be put down the drain, which is a
>waste.

No it doesn't, and no it isn't. You should reuse it - use the 2nd 
wash water for the next batch first wash, the 3rd wash water for the 
next batch 2nd wash and so on. So you're using each wash three times, 
only the 3rd wash is fresh. The first wash can't be reused, but it 
doesn't have to go down the drain either. A simple grey-water system 
will handle it well. We currently feed it to water hyacinths and 
duckweed, and compost the plants. Next step will be to reclaim 
cleansed water from the water hycinths and duckweed.

>In either case, the final glycerol can be pH
>neutralised with H3PO4 under closed loop control,
>the Sodium Phosphate precipitate removed via
>centrifuge, the water and ME separated via
>centrifuge. The final product is clear ME,
>neutral Glycerol and a compact solid fertilizer
>base.

If you believe in "fertilizers". Even if you do, mopst phosphates are 
applied to phosphate-rich soil, and most of what's applied quickly 
becomes unavailable to plants, like the rest. Phosphates are made 
available by biological action via the soil micro-life. Keep the 
micro-life happy and you don't need phosphates, nor any other 
"fertilizers".

Anyway, what do you mean by "neutral Glycerol"? You've accounted for 
the catalyst in the by-product cocktail, but not for the soap/FFA, 
which is probably most of it, and not for the excess methanol.

I don't understand the perceived need for centrifuges etc etc etc. 
What for? It increases the production rate? I don't think so - maybe 
it shortens the production *time*. Well, so what? Settling, washing, 
bubble-drying will take maybe 4-5 days from starting processing to 
finished, clear fuel. So if you have space to store 4-5 days' 
production, that's all you need. If you've got your processing right, 
that is - if you find a need for all this just for a "cleaner wash" 
it might help to pay some attention to optimizing your process. 
Whatever, what I've seen of centrifuges so far doesn't exactly 
impress, and nor does the price.

Best

Keith


>Mark
>
>=
>Mark Schofield
>M.Sc B.Eng DHE AMIMechE
>t 07944 401662
>e [EMAIL PROTECTED]
>Autogas Conversions and LPG Pumps


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