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PNNL-13501 - Pacific Northwest National Laboratory

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Study Control Number: PN00033/1440<br />

Development of In-Stack Reforming for Solid Oxide Fuel Cells<br />

Olga A. Marina<br />

The goal of this project was to evaluate anode materials and designs for the solid oxide fuel cell operating on partially<br />

pre-reformed hydrocarbons and develop <strong>Pacific</strong> <strong>Northwest</strong> <strong>National</strong> <strong>Laboratory</strong>’s capabilities to fabricate and test planar<br />

solid oxide fuel cells operating on partially pre-reformed hydrocarbon fuels.<br />

Project Description<br />

The primary objective of the project is to develop,<br />

fabricate, and test a thick porous anode that is compatible<br />

with other solid oxide fuel cell components, is coke<br />

resistant, exhibits excellent electrochemical properties,<br />

and has catalytic activity for internal reforming of<br />

methane. The development of such an electrode would<br />

allow solid oxide fuel cell stack operation on such<br />

inexpensive methane-containing fuels as natural gas or<br />

pre-reformed higher hydrocarbons, gasoline and diesel,<br />

provided they were desulfurized prior to use.<br />

Introduction<br />

For the solid oxide fuel cell with an yttria-stabilized<br />

zirconia electrolyte, a nickel-yttria-stabilized zirconia<br />

cermet is currently a favored anode material. State-ofthe-art<br />

Ni-yttria-stabilized zirconia anodes exhibit<br />

polarization resistance as low as 30 and 60 mΩcm 2 at<br />

1000 and 850 o C, respectively, in moist hydrogen<br />

(Primdahl and Mogensen 1999) and are being used<br />

successfully by most developers for solid oxide fuel cells<br />

operating on the clean reformed fuel. However, solid<br />

oxide fuel cells require the anode be tolerant to fuels less<br />

expensive than hydrogen hydrocarbon fuels (natural gas,<br />

gasoline) without external reforming. The major<br />

disadvantage of the nickel cermet electrode arises from<br />

the promotion of competitive catalytic cracking of<br />

hydrocarbons leading to rapid carbon deposition. Steam<br />

reforming of methane at high steam-to-carbon ratio<br />

potentially prevents sooting of the anode, but causes<br />

intolerable temperature gradients throughout the anode<br />

due to the high reactivity of nickel toward this reaction.<br />

Moreover, nickel is unsusceptible to an oxidizing<br />

atmosphere and is readily poisoned by sulfur, which is<br />

always present in the feedstock. Also, sintering of nickel<br />

on prolonged operation is a potential problem for any type<br />

of fuel (van Berkel et al. 1993).<br />

314 FY 2000 <strong>Laboratory</strong> Directed Research and Development Annual Report<br />

Application of internal reforming of methane in the solid<br />

oxide fuel cell offers several important advantages in<br />

comparison with external reforming: 1) no separate<br />

steam-reforming unit is needed; 2) smaller system size,<br />

lower equipment and operation costs, and lower capital<br />

investment are expected; 3) less cooling is required;<br />

4) less steam is required; 5) more evenly distributed<br />

hydrogen load; and 6) higher methane conversion are<br />

achieved. However, internal reforming also poses some<br />

flaws: 1) intolerable temperature gradients, 2) sooting,<br />

3) need to dilute fuel with steam in order to prevent<br />

carbon depositions, 4) recirculation and incomplete shift<br />

reaction adversely affect power generation, 5) gradual<br />

catalyst deactivation due to metal particle sintering, and<br />

6) additional catalysts may be required.<br />

Results and Accomplishments<br />

A comprehensive literature review was conducted to<br />

search for a new anode material and improvements of the<br />

traditional nickel cermet anode capable of in-stack<br />

reforming. Two promising research directions have been<br />

identified: redox tolerant anode concept, and a new anode<br />

for internal reforming.<br />

A multipurpose test rig was designed and built to enable<br />

anode materials testing in-house (see Figure 1). The test<br />

rig consisted of an electric furnace, a potentiostate, gas<br />

supplying/controlling system, and computer monitoring of<br />

anode and cathode temperatures. Electrolyte-supported<br />

cells can be tested both in hydrogen and methane by<br />

potentiometric and impedance spectroscopy techniques<br />

with the future possibility of simultaneous gas analyzing.<br />

<strong>PNNL</strong>’s cell fabrication technique was adopted for<br />

manufacturing two- and three-electrode cells for the test<br />

in that rig.

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