(503c) Catalytic Behavior in Internal Steam Reforming of Methane in SOFC Conditions over LaXSr2-XMnO4 Materials
AIChE Annual Meeting
2016
2016 AIChE Annual Meeting
Fuels and Petrochemicals Division
Unconventionals: Hydrogen and Fuel Cells II
Wednesday, November 16, 2016 - 9:10am to 9:30am
CATALYTIC
BEHAVIOR IN INTERNAL STEAM REFORMING OF METHANE IN SOFC CONDITIONS OVER LaXSr2-XMnO4
MATERIALS
Karen Silva1, Sebastian Vecino1*,
Monica Sandoval1, Patrick Gèlin2,
Paola Gauthier-Maradei1, Gilles
Gauthier1
1: INTERFASE,
Escuela de Ingeniería Química, Universidad Industrial de Santander, Carrera 27,
Calle 9 Ciudadela Universitaria, Bucaramanga, COLOMBIA
2: Université Lyon 1, CNRS, UMR 5256, IRCELYON, Institut de recherches sur la catalyse et lenvironnement de
Lyon, 2 avenue Albert Einstein, F-69626 Villeurbanne, France.
*e-mail:
jusevema13@hotmail.com
ABSTRACT
Nowadays, solid oxide fuel cells (SOFC) are one of the most attracting
and interesting energy conversion devices. They can convert the chemical energy directly to electrical energy with high
efficiency (>60%) and low environmental pollution, employing several types
of fuels such as hydrogen, coal gas, natural gas (methane) or another
hydrocarbons fuels. These electrochemical systems operate at high temperatures
(600-1000°C) using oxygen from the air as oxidant, and hydrogen directly or by
internal steam reforming (ISR) of some compounds present in the fuels to
produce heat as well as water and electricity. The ISR is a highly endothermic process
that takes place, catalytically, at the anode of the SOFC. However, during this
process and employing state of art anode material Ni/YSZ, the hydrocarbons
decompose into hydrogen and additionally in an undesired compound: solid carbon
(coke). This coke tends to deposit on the anode surface causing a rapid
deterioration of the cell due to the deactivation of catalytic activity and the
inhibition of hydrogen diffusion into the anode to continue with the
electrochemical reaction. In order to overcome this limitation, it is necessary
to develop new anode materials
that catalyse the ISR and reduce significantly the problem described
above. According to literature, single-phase oxide materials have been studied
with excellent results. In this work, La0.5Sr1.5MnO4 was studied as potential
new anodic material for SOFC directly fed with methane, operating at high
temperature and under water deficient conditions. The material was synthesized by Pechini method
and characterized by XRD. Measurements of catalytic activity
in steam reforming of methane were carried out using 40 mg of catalyst at 900°C
during 40h in a U-shaped quartz reactor. Different methane/water ratios
(0.66≤CH4/H2O≤10) were employed to determine kinetic parameters.
Coke formation during catalytic testing was measured by temperature programmed
oxidation (TPO). The catalytic activity was compared with a reference material
CGO (Ce0.9Gd0.1O2-d). Finally, the material was characterized again by
XRD to evidence any damage or changes in the catalyst structure. This catalyst
was found very active (high hydrogen production 9000ppmv) and resistant to coke formation (<69µmol/gcat), close to CGO catalyst (13000 ppmv hydrogen and 50.2µmol/gcat). The
materials present an excellent stability during the test run; no structural
change was found after the reaction. The small increase in the lattice
parameters was attributed to the manganese reduction during
the catalytic reaction (Mn+4/Mn+3 to Mn+3/Mn+2).
Key Words: Solid
oxide fuel cell, Internal steam reforming, Methane, Manganite, Energy.