Thanks Tom

 

 

 

From: Gasification [mailto:[email protected]] On 
Behalf Of l
Sent: Sunday, April 23, 2017 11:13 AM
To: [email protected]
Subject: SPAM: Re: [Gasification] SPAM: Re: SPAM: Re: Naphthalene Condensate 
Photos, GAST methodology

 

Tom,
    The NOx and CO ambient levels make the engine exhaust testing irrelevant, 
which is my point. As an example to put an engine/generator in service under 
EPA rules, the NOx must be below 3 ppm which may be below ambient, so that no 
one can operate an IC engine and compete with power companies. 
    I mean high carbon yield as char is high in carbon and reflects poor 
conversion efficiency. Ash is ash and if good ash, low in carbon. 
    We have not conducted specific tar analysis but have testing by Cummins in 
1983 showing acceptable engine cleanliness after operation. 
    

 

 

Sincerely,

Leland T. "Tom" Taylor

Thermogenics Inc. 

+001-505-463-8422 

www.thermogenicx.com <http://www.thermogenicx.com> 

Skype: ltt.invent

 

 

-----Original Message-----
From: Tom Miles <[email protected] <mailto:[email protected]> >
To: 'Discussion of biomass pyrolysis and gasification' 
<[email protected] 
<mailto:[email protected]> >
Sent: Sun, Apr 23, 2017 11:52 am
Subject: Re: [Gasification] SPAM: Re: SPAM: Re: Naphthalene Condensate Photos, 
GAST methodology

What are your target gas quality numbers? Can you meet them?

 

You likely mean high ash/char yield, rather than high carbon yield. 

 

Do you have data showing the impact of ambient NOx or CO on engine missions? 

 

 

 

From: Gasification [mailto:[email protected] 
<mailto:[email protected]?> ] On Behalf Of l
Sent: Sunday, April 23, 2017 9:19 AM
To: [email protected]
Subject: SPAM: Re: [Gasification] SPAM: Re: Naphthalene Condensate Photos, GAST 
methodology

 

Which data? Caterpillar isn't excited about produced gas operating engines? Not 
sure how I do that. 

 

 

Sincerely,

Leland T. "Tom" Taylor

Thermogenics Inc. 

+001-505-463-8422 

www.thermogenicx.com <http://www.thermogenicx.com> 

Skype: ltt.invent

 

 

-----Original Message-----
From: Tom Miles <[email protected] <mailto:[email protected]> >
To: Discussion of biomass pyrolysis and gasification 
<[email protected] 
<mailto:[email protected]> >
Sent: Sat, Apr 22, 2017 11:04 pm
Subject: Re: [Gasification] SPAM: Re: Naphthalene Condensate Photos, GAST 
methodology

Can you show us some data?

T R Miles Technical Consultants Inc. 

[email protected] <mailto:[email protected]> 

Sent from mobile. 


On Apr 22, 2017, at 9:51 PM, l <[email protected] <mailto:[email protected]> > 
wrote:

One of the major reasons Caterpillar won't get heavily involved in producer gas 
engines is the naphthalene issue. One group that had an operating power plant 
for a municipality would operate their engines for a few hundred hours and the 
valves would begin knocking and the V-12 engine would have to have a valve job. 
ir
    It is fairly easy to fix if one knows the properties of the gas. We do it 
as a matter of course as it doesn't make any sense to offer a system that has 
to have the engine rebuilt periodically. One engine manufacturer will not 
guarantee their engine unless it meets their strict standards.
    As to the GAST report, I read some of it and some of the procedures can 
easily be improved such as measuring the air inlet flow using a typical 
mass:flow meter out of a car that is extremely accurate and can provide 
continuous monitoring. In the program we use for our systems, it automatically 
calculates the inlet air flow rate and with settable or automatic monitoring 
inputs such as temp, humidity, can provide continuous and accumulated air mass 
input. 
    There are also methods of measuring gas composition, to much better detail 
than is now being used. Fixed gases such as the usual by either GC or specific 
gas analyzers do not show the condensable gases such as ethanol, methanol, 
acetone, acetic acid, napthalene of course, and other compounds that may affect 
engine operation for the better or worse. The same system could be used for 
engine exhaust measuring of say formaldehyde, carcinogens, and everything 
except PAH and particulate. 
    None of the gasifiers monitored are as efficient as we would like to see in 
our designs. High carbon yield in the char/ash residue is an admission of the 
inefficiencies present. 

    As another note, virtually all emission testing is flawed because if the 
inlet air has a few ppm of NOx or CO, the output is going to be biased upward 
this amount and none of the EPA testing protocols take ambient air quality into 
account. 

 

Sincerely,

Leland T. "Tom" Taylor

Thermogenics Inc. 

+001-505-463-8422 

www.thermogenicx.com <http://www.thermogenicx.com> 

Skype: ltt.invent

 

 

-----Original Message-----
From: Doug <[email protected] <mailto:[email protected]> >
To: 'Discussion of biomass pyrolysis and gasification' 
<[email protected] 
<mailto:[email protected]> >
Sent: Sat, Apr 22, 2017 5:39 pm
Subject: [Gasification] Naphthalene Condensate Photos

 

Naphthalene in Producer Gas

 

Hi Gasification Colleagues,

Reading through the Italian Paper on gasifier monitoring in South Tyrol, the 
reference to Naphthalene caught my eye, because as a light pyrolysis oil, after 
dry filtration and condensation, I have only seen this in gas in the Northern 
hemisphere. Looking like yellow oil floating on aqueous condensate,  exposed to 
air when tipped onto a concrete surface, it just completely vaporizes leaving 
only a carbon trace of stain. It makes a good mess inside pipes and diaphragm 
regulators and if being combusted in a flare or oxidation chamber, will add to 
the emissions from the stack. The bottom line is that we don't want this in our 
producer gas for either engine or combustion applications, but once condensed, 
it's very hard to clean out of the gas.

My questions to any one who might have some similar experience, is why 
Naphthalene may not show up in small gasifiers under say 100m3/hr, yet becomes 
a issue as the gas output increases from a larger system. I have observed this 
formation in N.Ireland and California and definitely related to just higher 
output. Could it be related to the amount or volume of the unstable pyrolysis 
gas in the fuel hopper? Can this create a chemistry that can survive an 
incandescent char bed, but reform as Naphthalene in the gas reduction phase? 

I can assure you that it isn't about tar or bad design, as our bed analysis and 
pressure drop continuous monitoring has not shown bridging or channeling to be 
the culprit. Black tars are never present, nor is CH4  as Methane (<2%), so bed 
temperatures are not an issue, nor moisture content of the fuels (wood chips or 
blocks). Char under the grate is dry and clean, as is the <10 micron dust from 
the cyclones.

The photos show two samples from a larger system, one a first stage cooling 
containing ash and carbon with a purple colour from the ash. The second bag 
from the cooling condenser is yellow from the Naphthalene which did increase 
with more gas output . The square container is completely clear and comes from 
the Fluidyne  Pacific Class gasifier (90m3/hr) and it has always made clear 
condensate in both hemispheres except when incorrectly fueled. It has not been 
possible to test larger gasifiers of our own design here in New Zealand, hence 
the questions.

Any discussion would be appreciated.

Doug Williams,

Fluidyne.

 

 

 

  

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