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Solid oxide fuel cells tubular type

There are many chemically reacting flow situations in which a reactive stream flows interior to a channel or duct. Two such examples are illustrated in Figs. 1.4 and 1.6, which consider flow in a catalytic-combustion monolith [28,156,168,259,322] and in the channels of a solid-oxide fuel cell. Other examples include the catalytic converters in automobiles. Certainly there are many industrial chemical processes that involve reactive flow tubular reactors. Innovative new short-contact-time processes use flow in catalytic monoliths to convert raw hydrocarbons to higher-value chemical feedstocks [37,99,100,173,184,436, 447]. Certain types of chemical-vapor-deposition reactors use a channel to direct flow over a wafer where a thin film is grown or deposited [219]. Flow reactors used in the laboratory to study gas-phase chemical kinetics usually strive to achieve plug-flow conditions and to minimize wall-chemistry effects. Nevertheless, boundary-layer simulations can be used to verify the flow condition or to account for non-ideal behavior [147]. [Pg.309]

In this code, a 1-dimensional electrochemical element is defined, which represents a finite volume of active unit cell. This 1-D sub-model can be validated with appropriate single-cell data and established 1-D codes. This 1-D element is then used in FLUENT, a commercially available product, to carry out 3-D similations of realistic fuel cell geometries. One configuration studied was a single tubular solid oxide fuel cell (TSOFC) including a support tube on the cathode side of the cell. Six chemical species were tracked in the simulation H2, CO2, CO, O2, H2O, and N2. Fluid dynamics, heat transfer, electrochemistry, and the potential field in electrode and interconnect regions were all simulated. Voltage losses due to chemical kinetics, ohmic conduction, and diffusion were accounted for in the model. Because of a lack of accurate and detailed in situ characterization of the SOFC modeled, a direct validation of the model results was not possible. However, the results are consistent with input-output observations on experimental cells of this type. [Pg.83]

Figure 7.25 End view of tubular type solid oxide fuel cell produced by Siemens Westinghouse. The electrol5de and the anode are built onto the air cathode. Figure 7.25 End view of tubular type solid oxide fuel cell produced by Siemens Westinghouse. The electrol5de and the anode are built onto the air cathode.
A. Kawakami, S. Matsuoka, N. Watanabe, A. Ueno, T. Ishihara, N. Sakai, K. Yamaji, H. Yokokawa, Development of low-temperature micro tubular type SOFC. Proceedings of the 13th Symposium on Solid Oxide Fuel Cells in Japan, 54-57 (2004)... [Pg.216]


See other pages where Solid oxide fuel cells tubular type is mentioned: [Pg.584]    [Pg.59]    [Pg.18]    [Pg.348]    [Pg.179]    [Pg.33]    [Pg.203]    [Pg.211]    [Pg.223]    [Pg.141]    [Pg.1353]    [Pg.205]    [Pg.197]    [Pg.267]    [Pg.16]   
See also in sourсe #XX -- [ Pg.214 ]




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Fuel cells solid oxide

Fuel cells types

Fuel oxidation

Fuel solid oxide

Fuel type

Oxidant Type

Oxidants, solid

Oxidation cell

Oxidation solids

Oxide Fuel Cells

Oxide fuels

Oxides types

Oxidizing solid

Solid fuel cell

Solid fuels

Solid oxide

Solid oxide cells

Solid oxidizers

Solid types

Solide fuel cell

Tubular cells

Tubular solid oxide fuel cell

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