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PNNL-13501 - Pacific Northwest National Laboratory

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Simulation and Modeling of Electrochemistry and Performance Assessment of Solid Oxide<br />

Fuel Stacks<br />

Mohammad A. Khaleel, Kurt P. Recknagle, Z. Lin, John E. Deibler, John E. Jaffe, Rick E. Williford, Byung K. Ahn<br />

Study Control Number: PN00081/1488<br />

Development of methods for calculating current density, cell voltage, and heat production in planar solid oxide fuel cells<br />

(SOFC) stacks with various fuels is critical for coupling an electrochemical model and thermo-fluids and stress analysis.<br />

Project Description<br />

The objective of this project was to develop<br />

computational methods and simulation tools for<br />

predicting electrochemical behavior in SOFC stacks, and<br />

to gain a fundamental understanding of the effect of<br />

various operation conditions on the V-i relation. This<br />

project also was performed to provide analytical insight<br />

into the correlation between cell efficiency and fuel use.<br />

The technical work involved developing numerical<br />

procedures to simulate the heat generation from Joule<br />

heating and chemical reaction, and species production and<br />

destruction via mass balance to analyze the dependence of<br />

the Nernst potential on temperature and pressure. Also,<br />

the effect of having CO oxidation at the anode as an<br />

added contribution to the total current was investigated.<br />

Introduction<br />

Solid oxide fuel cells (SOFCs) produce direct current<br />

power from fuel and oxidant via an electrochemical<br />

process. The efficiency of such power generating<br />

methods compares favorably with conventional thermal<br />

power generation that is limited by Carnot-type<br />

constraints. Current SOFCs represent a highly developed,<br />

but immature technology. One advance necessary is to<br />

increase efficiency. Although the design and operation of<br />

a SOFC appears simple, many of the phenomena<br />

dominating the performance of a SOFC are complex,<br />

competing, and poorly understood; this is especially true<br />

of the electrochemistry. Mathematical models are<br />

required to incorporate the known physics and behavior of<br />

SOFC materials to predict and improve performance. It is<br />

well established that the cell direct current voltage and<br />

current depend on conditions that include fuel flow,<br />

oxidant flow, pressure, temperature, and the demands of<br />

the load circuit. These parameters affect the<br />

electrochemical processes that ultimately determine the<br />

generated power and cell voltage. By taking into account<br />

1) ohmic losses, 2) concentration polarization based on<br />

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

the assumption of binary diffusion of gaseous species<br />

through porous electrodes, and 3) Tafel-type activation<br />

polarization in composite electrodes, it is shown that the<br />

V versus i traces can be adequately described by:<br />

V(i) = E open – iR i – b sinh -1 (i/2i 0) + (RT/4F)ln(1-i/i O2) +<br />

(RT/2F)ln(1-i/i H2) – (RT/2F)ln[1+p 0 H2i/(p 0 H2Oi H2)]<br />

In the above equation, Eopen is the open circuit voltage,<br />

usually referred as Nernst potential. Ri is the area specific<br />

resistance of the cell, b is the Tafel parameter. iO2 and iH2<br />

are respectively the cathode- and anode-limiting current<br />

density, p 0 H2 and p 0 H2O are respectively the partial<br />

pressure of hydrogen and water vapor in the fuel channel,<br />

R is the gas constant, F is the Faraday constant, and T is<br />

the temperature.<br />

It should be noted, however, that the above equation is<br />

valid only for a SOFC using H2 as the input fuel. To<br />

accommodate multifuel capacity, which is one of the<br />

main advantages of SOFCs, modification is required.<br />

Fuels other than pure hydrogen generally contain CO,<br />

reacting with H2O to produce CO2, and this reaction needs<br />

to be included in the mathematical modeling for a more<br />

accurate electrochemistry analysis. At present, <strong>PNNL</strong> is<br />

in the process of including the CO effect in an alreadyestablished<br />

electrochemistry code programmed by current<br />

authors for pure hydrogen-fed SOFCs. This effort will<br />

soon be linked to FEA modeling using Marc to complete<br />

interfacing the electrochemistry analysis with the thermofluids<br />

and stress analysis.<br />

Results and Accomplishments<br />

Electrochemistry Modeling<br />

An electrochemistry code was written in Fortran based on<br />

Kim et al. (1999). Prior to the main analysis, dependence<br />

of Nernst potential on temperature and pressure has been<br />

examined, and the summary is listed below.

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