[Gasification] Syngas on Wiki_
Pannirselvam P.V
pannirbr at gmail.com
Tue Jan 4 16:16:02 CST 2011
Helo Leland TOm
This how we try to model tom make simple simple process where
indirect heated pyrolysis is made simultanely along with gasification
pyrolysis oil leading to Gas methane, C02 , CO which has to be shifted
using steam whch can increase the co2 along with H2. This reformed gas
obtained as co product of activated charcoal, methanol , unconverted
syngas for small CHP.
We also think of solid charcoal and methane , high temperature
pyrolysis alterative to H2:CO content to make less CO2 syngas
, suitable for small scale Biomass 2 liquid project such as GEK low cost
technology, to make multy products
On Mon, Jan 3, 2011 at 3:58 PM, <linvent at aol.com> wrote:
> An interesting thought on the naming of "syngas" is that if a gasifier
> produces "syngas" and then it has to be shifted in H2:CO content for a
> catalytic process, then what is it called?
ore con
This can be called as reformed gas /
The use of reforming , reformed gas can be the correct instead of
syngas
The use of pyrogas is very clear with repect to the product and process,
the same to for producer gas , when you come to syngas ,it can be defined by
the process , but only the product, making it use not specific
>
> Truely
>
Pannirselvam
> -----Original Message-----
> From: LINVENT <LINVENT at aol.com>
> To: gasification <gasification at bioenergylists.org>
> Sent: Tue, Dec 28, 2010 5:00 pm
> Subject: Re: [Gasification] Syngas on Wiki_
>
> I believe that syngas is specific to the application, and is based on the
> ratio of hydrogen to carbon monoxide. As an example, ammonia syngas as
> defined in flow sheets for an ammonia plant is 3H2:1N2. Syngas for FT
> reactions
> can be from .6H2:1CO-1.5H2:CO, with iron based catalysts requiring less H2
> than cobalt catalysts because the iron catalyst will do it's own shift
> reaction. Produced gas, water gas, blue gas, low heating value gas, low CV
> gas are
> all more appropriate designations for air based gasification systems. Even
> an
> oxygen or steam driven gasification system will not produce a "syngas"
> appropriate for certain catalyst reactions, but will work for many.
>
> The use of nitrogen in the gas is indeed done in some of the more
> sopshisticated catalyst systems because it reduces the thermal
> concentration
> in the
> typically exothermic reactor such as FT reactions which in turn reduces the
> amount of cooling needed for the reactor design which can be a significant
> effect.
>
> The use of the term "syngas" is inappropriate for any gasification system
> because it is a specific composition based on the catalyst used. Only
> syngas
>
> can be called this when it is cleaned, balanced for the catalyst with
> contaminants removed such as Cl, S, organics so that the catalyst is not
> damaged
> by it.
>
>
>
> Sincerely,
> Leland T. "Tom" Taylor
> President
> Thermogenics Inc.
> 505.463.8422
> www.thermogenics.com
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--
************************************************
P.V.PANNIRSELVAM
ASSOCIATE . PROF.
Research Group ,GPEC, Coordinator
Computer aided Cost engineering
DEQ – Departamento de Engenharia Química
CT – Centro de Tecnologia / UFRN, Lagoa Nova – Natal/RN
Campus Universitário. CEP: 59.072-970
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