Not all plasma systems are identical so it's not necessarily correct to think 
of plasma gasification as an environment of intense heat. Systems like those 
promoted by AlterNRG/Westinghouse maintain intense temperatures in the ash bed 
but the gases must travel up through a cooler pile of pyrolyzing fuel in which 
many of the inorganic components would condense. The top of the fuel pile looks 
like any other updraft gasifier except that by using the plasma to maintain the 
process (3% of heat input) you use less air. There are waste plasma gasifier 
coupled to boilers in Japan. 

Tom



-----Original Message-----
From: [email protected] 
[mailto:[email protected]] On Behalf Of 
[email protected]
Sent: Sunday, February 12, 2012 7:45 AM
To: [email protected]
Subject: Re: [Gasification] Hazardous classification of MSW, plasma 
gasification thermodynamics

GAsification produces an ash where the RCRA hazardous metals are bound and 
inert,  and pass US EPA TCLP leachate test which means that it can be put into 
landfill. I am not sure how MSW can be classed as a hazardous waste as per your 
language Peter. Otherwise normal landfills would also accept hazardous waste. 
Metals volatilized in a normal gasifier are condensed in the lower temperature 
section of the gas processing. In plasma gasification they would coat any 
nearby cooler surface very rapidly, leading to potential blockage in short 
order. The amount of energy put into plasma gasification is a waste of energy 
as all of the desired reactions occur at much lower temperature and it makes no 
thermodynamic reason to go above those temperatures. Ash vitrification in 
plasma is supposedly better, but the lower temperature and hydrogen environment 
of a regular gasifier produce a stable TCLP ash anyhow.
There are direct methods of measuring metals in a gas stream. There is an 
interesting study where the metal balance in a gasifier is attempted to be 
determined but couldn't. More went in  than came out and where the difference 
occurred was never determined.
Sincerely,
Leland T. "Tom" Taylor
President
Thermogenics Inc.

-----Original Message-----
From: jonathan <[email protected]>
To: Discussion of biomass pyrolysis and gasification 
<[email protected]>
Sent: Sat, Feb 11, 2012 7:39 pm
Subject: Re: [Gasification] Steam Turbines

We can provide custom turbines; if you will forward your requirements I'll 
provide you with a quote.

Thanks,


Jonathan

On Sat, Feb 11, 2012 at 3:58 PM, Peter & Kerry 
&lt;[email protected]&gt; wrote:
Hi Liran,

The 2 second combustion requirement is an Interesting and slightly disturbing 
prescriptive regulator response (that narrows gas use options), is somebody in 
authority just guessing and being cautious or is it based around actual gas 
analysis results from your plasma gasification system?

What potential constituents in the gas stream are these requirements aimed at?

In regard our own experience with gasifying hazardous waste (sewerage sludge 
with potential heavy metal contaminants, particularly mercury &
cadmium) the client at the time for this (a large public authority) would not 
pay for direct emissions testing covering these so we paid out of our own 
pockets for an indirect "indicator" measurement, getting a ultimate analysis of 
the raw feed stock and the same test on the ash collected from the test run, 
then had a industrial chemist review the results. This showed the metals 
identified in the original analysis were captured within the ash in equivalent 
amounts relative to the mass reduction from the original sample (so didn't 
travel out with the gas).

Is this a problem with Plasma gasification? Are such contaminants mobilised in 
the gas instead?

We are currently engaged in the early stages of a formal testing project 
involving MSW and other hazardous wastes that will have EPA oversight and 
permitting for the trial. The results from this will inform pilot commercial 
scale system design and operating parameters in regard to emission management 
for our own system, so we are interested in what other regulator agencies are 
thinking in regard general gasification issues that might be flagged along the 
way.

Otherwise we would agree with Pannierselvam's question. Certainly subject to 
your gas meeting all the requirements for gas turbines (not just energy 
content) then these combined with downstream HRSG steam units using this 
exhaust, perhaps augmented with some  auxiliary firing if needed, could be 
another way to meet your regulatory requirement.

At the moment we are unaware of any commercial fuel cells that wouldn't require 
a high level of gas polishing and separation without quickly poisoning the 
cell, but also would love to hear more.

Regards,
Peter

Peter Davies
Real Power Systems Pty Ltd
Australia


Steam Turbines

Liran Dor liran at eer-pgm.com
Sat Feb 11 13:26:27 CST 2012
Previous message: [Gasification] Steam Turbines Messages sorted by: [ date ] [ 
thread ] [ subject ] [ author ] Dear Pannierselvam,

Thank you for your reply

The reason for the rankin cycle is that due to the fact we are treating 
hazardous waste the environmental regulation dictate we combust the gas in a 
chamber with a 2 second residence time.

I do like your approach for the MSW application we are working on and would 
like to hear more about it.

Thanks

Liran


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