REPP logo banner adsolstice ad
site map
Google Search REPP WWW register comment
home
repp
energy and environment
discussion groups
calendar
gem
about us
employment
 
REPP-CREST
1612 K Street, NW
Suite 202
Washington, DC 20006
contact us
discussion groups
efficiencyefficiency hydrogenhydrogen solarsolar windwind geothermalgeothermal bioenergybioenergy hydrohydro policypolicy
Gasification Archive for March 2001
158 messages, last added Tue Nov 26 17:17:42 2002

[Date Index][Thread Index]

GAS-L: Syngas genset




Hi Ariel;

I have reformatted your chart by "guess" -- could you verify if this is
correct?

One question -- your gas products appear to be the result of steam
reformations under 3 differing conditions. Probably just temperature?
Methane being the product of steam reformation at lower temperatures.

What process are you using and with what carbon material as charge?

Could you enlighten us please?

Peter Singfield

****reformat of original message******

Hello,

I have noticed the syngas composition did not go through so I am re-sending
my inquiry:

I am running an experiment of producing syngas (Gas rich with Hydrogen) and
feeding it to a reciprocating gas engine, the composition of the syngas
varies according to the process temperature from syngas I to syngas III as
follows:. 
   
Composition [moll - %]            
Gas                                                     Syngas I
Syngas II        Syngas III

Methane                                               0.296037
0.14331           0.020385
Carbon Monoxide                                  0.038796         0.100443
0.189042
Carbon Dioxide                                     0.185704         0.14857
0.088326  
Hydrogen                                             0.477759
0.607774          0.702234

Density                                                    6.22
5.35                  4.54
Net heating value (60 Deg. F) [kj/kg]          24353             22592
21968
Vol. LHV [kj/m^3]                                   151398            120783
99694

The gas conditions are at 25 Deg. C and 10 bar

The gas can be supplied at 10-50 Deg. C and at constant pressure in the
range of 10-15 barg to the engine.
If needed it is also possible to start the engine with liquid fuel or LPG
and then change over to the syngas.

The area the engine will be placed is classified as Class 1 Div.2 Group B
because of the Hydrogen presence.
The electrical output of the engine should be in the range of 100-400
kWe.(No heat recovery needed)

Can anyone direct me to a company that could supply a gas engine that could
stand in this specifications?



Regards,
Ariel Rotstein
R&D Dept.

Ormat Industries Ltd.
Box 68.
Yavne, 81100

Israel
Tel:  972-8-9433860
Fax: 972-8-9439901
e-mail: arotstein@ormat.com 





Gasification List is sponsored by
USDOE BioPower Program http://www.eren.doe.gov/biopower/
and PRM Energy Systems http://www.prmenergy.com
-
Other Sponsors, Archives and Information
http://www.nrel.gov/bioam/
http://www.crest.org/renewables/gasification-list-archive
http://solstice.crest.org/renewables/biomass-info/gasref.shtml
http://www.crest.org/renewables/biomass-info/
http://www.crest.org/renewables/biomass-info/carbon.shtml