Tom 

I can Imagine Weiss gave interesting information before they started their 
gasifier.

I visited 4 Ankur gasifiers in Sri Lanka 2 years ago - the main problem was not 
the gas cleaning but that the gasifier core lifetime was a few hundred hours. 

I can only agree that for small systems steam systems looks as the most 
reliable way to produce electricity

Thomas

-----Oprindelig meddelelse-----
Fra: Gasification [mailto:[email protected]] På 
vegne af Tom Miles
Sendt: 1. december 2013 00:35
Til: 'Discussion of biomass pyrolysis and gasification'; 'Kevin'
Emne: Re: [Gasification] Fluidised bed reactor

Thomas,

I have written to Weiss about their status. Nothing on the internet seems to be 
current. Last year they gave us some interesting information when we were 
looking at the feasibility of a 2 MWe gasifier for a village in Alaska. 

There is still a need for affordable and reliable systems operating at 
capacities less than 5 MWe. Steam systems with either combustion or 
gasification still seem to be the most dependable and lowest cost  systems 
considering capital and operating costs. 

I understand that Ankur has improved their gas cleaning and have been selling  
large (1-2 MWe) systems in South Asia. I haven't seen performance reports for 
anything besides their large flagship plant in India. 

In our economy FB gasifiers are most suited to larger systems (>5 MWe). 

Tom

-----Original Message-----
From: Gasification [mailto:[email protected]] On 
Behalf Of Thomas Koch
Sent: Saturday, November 30, 2013 12:34 AM
To: Discussion of biomass pyrolysis and gasification; 'Kevin'
Subject: Re: [Gasification] Fluidised bed reactor

Tom 

I agree very much to your description of the status of FB gasifiers. 
Not real upscaleable to an interesting size  - to many operations problems - 
too big carbon or thermal losses and too dirty gas to real interesting !
The 2 Danish FB biomass gasifier - Pyroneer and Skive are struggling a real lot 
with gas cleaning. 

Do you have any idea of the status of the Viking gasifier development? 

I have asked several times if it is possible to visit the plant for over 2 
years - or if there is a public report available with a little data?? but no 
luck sofar.  

The last information I have from the project is from linked-in where saw that 
the only engineer I knew on the project have left  this summer. 

Best regards

Thomas Koch 


-----Oprindelig meddelelse-----
Fra: Gasification [mailto:[email protected]] På 
vegne af Tom Miles
Sendt: 30. november 2013 07:01
Til: 'Kevin'; 'Discussion of biomass pyrolysis and gasification'
Emne: Re: [Gasification] Fluidised bed reactor

If you want to use the engine exhaust in a gasifier you must consider the heat 
and material balance for a gasifier and IC engine. 

Fuel input 100%
Heat loss in FB gasifier 5%
(Sensible) Heat loss to cooling the gas 25% Cold clean gas efficiency to engine 
70% (20% C0, 20% H2, 2% CH4, 12% CO2, 44% N).
Heat conversion in engine ~25%
33% to power (~14-17% fuel to power)
33% to engine jacket heat (17% net)
33% to exhaust. (17% net, mostly CO2 and N)

By injecting exhaust into the gasifier you are recycling a lot of inert gas 
(CO2, N2) and very little heat. The best use of the exhaust gas heat may be in 
preconditioning the fuel. Danish Technological University (DTU Viking gasifier, 
1990-2010,  that is now being commercialized by Weiss) and later All Power Labs 
(Power Pallet, 2009) have used heat from the exhaust to indirectly dry and 
pyrolyze incoming fuel. The dried and partially devolatilized wood, along with 
preheated combustion air, appears to contribute to a stable oxidation zone. 
Both units make a very good quality gas. These are both fixed bed downdraft 
gasifiers with pre-pyrolysis zones.
Peak temperatures reach 1000 C-1200 C in the oxidation zone and 800-900C in the 
reduction zones. 
http://www.btgworld.com/en/references/publications/handbook-biomass-gasifica
tion-second-edition

We have worked with many fluidized bed gasifiers in research and in industrial 
applications, for producer gas, and for synthesis gas. The fluidized bed is an 
intriguing reactor that has its use in industrial applications but they are 
expensive to build and operate.

Fluidized bed (FB) gasifiers are unique because distributor plates or nozzles 
in the bed uniformly distribute the reactant (air, steam) in the sand (or 
media) bed. It is therefore imperative that the fuel be distributed uniformly 
for good gasification. This good distribution affords good temperature control 
as the fuel goes through the exo- and endo- thermic reactions that Kevin 
described. The ideal arrangement is to feed the fuel into the bed and allow 
sufficient time (depth) for it to completely react before breaking the surface 
into the vapor space above the bed. Of course there are variations on fluidized 
bed reactors such as spouted beds, fast beds, or entrained flow reactors. The 
latter are used for fast pyrolysis to liquid fuels by companies like Ensyn. I 
think that Dynamotive is the only company that uses a bubbling bed for 
pyrolysis. Many of the biomass to liquid reactors consumes the char to drive 
the process so there is no excess char 

When used for gasification fluidized beds can be pretty stable in the
650-750 C range. The higher temperatures are needed to provide thermal inertia 
when wetter fuel (>20% MC) is used. Higher temperatures are generated by adding 
oxidants as Kevin has described. Higher vapor space temperatures (750 C) can be 
achieved by adding air above the bed. The partial oxidation can reduce NOx 
precursors in the fuel gas. You can think of the heat balance as consuming 
between 25% and 33% of the fuel to convert the remainder to chemical (producer 
gas or syngas) and sensible energy.
Producer gas is burned directly in a boiler or reformed for use in engines.
Synthesis gas is usually made using enriched air or oxygen as the reactant or 
by indirect heating, as in a dual fluid bed. The variety of catalytic reformers 
used to make synthesis gases can be seen online in the presentations at the TC 
Biomass 2011 and 2013 conferences.
http://www.gastechnology.org/tcbiomass2013/Pages/2013-Presentations.aspx

There are a few small commercial (50-100 tpd) fluidized bed/entrained flow 
pyrolyzers that are making specialized products (liquid smoke) for the food 
industry. In general there are no commercial small scale fluidized bed 
gasifiers or combustors.
Attempts by US boiler makers and several small entrepreneurs have failed to 
sustain commercial operation of fluidized bed gasifiers or combustors at the 
small scale. 

Tom  Miles
  

  

   





-----Original Message-----
From: Gasification [mailto:[email protected]] On 
Behalf Of Kevin
Sent: Friday, November 29, 2013 9:23 AM
To: Discussion of biomass pyrolysis and gasification
Subject: Re: [Gasification] Fluidised bed reactor

Dear Rex

----- Original Message -----
From: "Rex Zietsman" <[email protected]>
To: <[email protected]>
Sent: Friday, November 29, 2013 4:18 AM
Subject: [Gasification] Fluidised bed reactor


> Kevin,
>
> What you say is correct. However, there is benefit in returning some 
> exhaust back to gasification as you force a higher production of CO 
> relative to
> CO2
> production. I suspect it is an equilibrium thing...

# For a gasifier having a relatively high exit temperature, then engine exhaust 
additions to the gasifier intake air could indeed be a way to both lower the 
gasifier exit temperature, and to raise the CO level.

There is a CO/CO2 equilibrium consideration, and also a kinetics or "speed of 
reaction" consideration.

Best wishes,

Kevin
>
> Rex
>
>
> ---
> This email is free from viruses and malware because avast! Antivirus 
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> http://www.avast.com
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