H2O2-fuel cells fed with a H2N2-mixture and air
Identifieur interne : 000513 ( Istex/Curation ); précédent : 000512; suivant : 000514H2O2-fuel cells fed with a H2N2-mixture and air
Auteurs : D. Sprengel [Allemagne]Source :
- Energy Conversion [ 0013-7480 ] ; 1975.
English descriptors
- Teeft :
- Ammonia, Ammonia cracker, Cascade, Cascade step, Current density, Current density function, Decomposed hydrazine, Density function, Diffusion electrodes, Energy conversion, Energy weight, Equal importance, First cascade step, Flow chart, Fuel cell, Fuel cell batteries, Fuel cell battery, Hydrazine, Hydrazine decomposer, Hydrazine hydrate, Input signal, Last cell, Liquid ammonia, Loss factor, Normal output, Outlet concentration, Purge, Raney nickel catalyst, Reaction water, Second step, Signal voltage, Soda lime, Steel cylinders, Sudden reduction, Terminal voltage, Third cascade step, Transient response, Waste heat, Winsel, Xout.
Abstract
Abstract: Considering the large weight of gas cylinders (for compressed gases) the advantage of fuel stored in the liquid state is obvious, e.g. liquid NH3, which may be cracked into a H2N2 mixture.The nitrogen in the gas mixture requires a special arrangement of the gas flow within the battery when using Raney nickel catalyst. Besides this arrangement a device that controls the nitrogen concentration is necessary. In order to obtain a trouble-free gas flow arrangement some numerical relations have to be observed.A 100 W fuel cell aggregate operated by air and a H2N2 mixture serves as example.
Url:
DOI: 10.1016/0013-7480(75)90048-0
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<author><name sortKey="Sprengel, D" sort="Sprengel, D" uniqKey="Sprengel D" first="D." last="Sprengel">D. Sprengel</name>
<affiliation wicri:level="1"><mods:affiliation>c/o VARTA Batterie AG, Forschungs- und Entwicklungs-Zentrum, D-6233 Kelkheim/Taunus, Postfach 206, F.R. Germany</mods:affiliation>
<country xml:lang="fr" wicri:curation="lc">Allemagne</country>
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<sourceDesc><biblStruct><analytic><title level="a">H2O2-fuel cells fed with a H2N2-mixture and air</title>
<author><name sortKey="Sprengel, D" sort="Sprengel, D" uniqKey="Sprengel D" first="D." last="Sprengel">D. Sprengel</name>
<affiliation wicri:level="1"><mods:affiliation>c/o VARTA Batterie AG, Forschungs- und Entwicklungs-Zentrum, D-6233 Kelkheim/Taunus, Postfach 206, F.R. Germany</mods:affiliation>
<country xml:lang="fr" wicri:curation="lc">Allemagne</country>
<wicri:regionArea>c/o VARTA Batterie AG, Forschungs- und Entwicklungs-Zentrum, D-6233 Kelkheim/Taunus, Postfach 206</wicri:regionArea>
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<series><title level="j">Energy Conversion</title>
<title level="j" type="abbrev">ENCONV</title>
<idno type="ISSN">0013-7480</idno>
<imprint><publisher>ELSEVIER</publisher>
<date type="published" when="1975">1975</date>
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<profileDesc><textClass><keywords scheme="Teeft" xml:lang="en"><term>Ammonia</term>
<term>Ammonia cracker</term>
<term>Cascade</term>
<term>Cascade step</term>
<term>Current density</term>
<term>Current density function</term>
<term>Decomposed hydrazine</term>
<term>Density function</term>
<term>Diffusion electrodes</term>
<term>Energy conversion</term>
<term>Energy weight</term>
<term>Equal importance</term>
<term>First cascade step</term>
<term>Flow chart</term>
<term>Fuel cell</term>
<term>Fuel cell batteries</term>
<term>Fuel cell battery</term>
<term>Hydrazine</term>
<term>Hydrazine decomposer</term>
<term>Hydrazine hydrate</term>
<term>Input signal</term>
<term>Last cell</term>
<term>Liquid ammonia</term>
<term>Loss factor</term>
<term>Normal output</term>
<term>Outlet concentration</term>
<term>Purge</term>
<term>Raney nickel catalyst</term>
<term>Reaction water</term>
<term>Second step</term>
<term>Signal voltage</term>
<term>Soda lime</term>
<term>Steel cylinders</term>
<term>Sudden reduction</term>
<term>Terminal voltage</term>
<term>Third cascade step</term>
<term>Transient response</term>
<term>Waste heat</term>
<term>Winsel</term>
<term>Xout</term>
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<langUsage><language ident="en">en</language>
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<front><div type="abstract" xml:lang="en">Abstract: Considering the large weight of gas cylinders (for compressed gases) the advantage of fuel stored in the liquid state is obvious, e.g. liquid NH3, which may be cracked into a H2N2 mixture.The nitrogen in the gas mixture requires a special arrangement of the gas flow within the battery when using Raney nickel catalyst. Besides this arrangement a device that controls the nitrogen concentration is necessary. In order to obtain a trouble-free gas flow arrangement some numerical relations have to be observed.A 100 W fuel cell aggregate operated by air and a H2N2 mixture serves as example.</div>
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