OcrV1, PascalFrancis, Curation, bibRecord, 000621

Performance of SOFC coupled with n-C4H10 autothermal reformer: Carbon deposition and development of anode structure

Identifieur interne : 000621 ( PascalFrancis/Curation ); précédent : 000620; suivant : 000622

Performance of SOFC coupled with n-C4H10 autothermal reformer: Carbon deposition and development of anode structure

Auteurs : Gyujong Bae [Corée du Sud] ; Joongmyeon Bae [Corée du Sud] ; Pattaraporn Kim-Lohsoontorn [Corée du Sud, Thaïlande] ; Jihoon Jeong [Corée du Sud]

Source :

International journal of hydrogen energy [ 0360-3199 ] ; 2010.

RBID : Pascal:11-0087936

Descripteurs français

Pascal (Inist)
- Performance, Pile combustible, Pile combustible oxyde solide, Anode, Nickel, Zircone, Oxyde de zirconium, Lanthane, Reformage vapeur, Oxydation partielle, Vapeur eau, Hydrocarbure, Mélange gaz, Conductivité électrique, Oxyde de cérium, Cobalt, Ferrite, Samarium, Catalyseur, Rhodium, Processus reformage autothermique, Hydrogène.
Wicri :
- topic : Nickel, Hydrocarbure, Cobalt, Hydrogène.

English descriptors

KwdEn :
- Anode, Autothermal reformer processes, Catalyst, Cerium oxide, Cobalt, Electrical conductivity, Ferrite, Fuel cell, Gas mixture, Hydrocarbon, Hydrogen, Lanthanum, Nickel, Partial oxidation, Performance, Rhodium, Samarium, Solid oxide fuel cell, Steam reforming, Water vapor, Zirconia, Zirconium oxide.

Abstract

The performance deterioration of solid oxide fuel cells (SOFCs, Nickel-Yttria stabilized zirconia (Ni-YSZ)/YSZ/lanthanum doped strontium manganite-YSZ (LSM-YSZ)) coupled with n-C₄H₁₀ steam reformers (SR), autothermal reformers (ATR), or catalytic partial oxidation reformers (CPOX) was examined using an integrated system of a micro-reactor reformer and SOFC unit. The terminal voltage rapidly degraded in CPOX-driven SOFC (oxygen to carbon ratio (OCR) = 0.5) while it was fairly stable for SR-driven SOFC (steam to carbon ratio (SCR) = 2) over 250 h. For ATR-driven SOFC at near the thermoneutral point (OCR = 0.5 and steam to carbon ration (SCR) = 1.3), significant deterioration of the terminal voltage was observed in 100 h of operation. The main precursors of carbon deposition on the SOFC were identified by reformate gas analysis during the tests. In this study, we reveal that the carbon deposition on the SOFC anode can be affected by not only lower-order hydrocarbons (C₁C₄), but also by the CO/H₂ gas mixture. The change in electrical conductivity of the Ni-YSZ cermet used for the SOFC anode was investigated under different gas mixtures. To investigate the propensity for carbon deposition by each carbon-containing gas mixture, we defined the ratios of steam to specific carbon (C₁C₄ lower-order hydrocarbons and CO) in the reformate gas (SSCR, steam to specific carbon ratio). To inhibit carbon deposition on SOFC anode, the SSCR must be sufficiently high. However, the reformer operates near its maximum efficiency at low SSCR value and the higher the SSCR value, the lower the open circuit voltage and operating power density due to Nernst potential. In this study, a metal-foam supported SOFC single cell (Ni-YSZ/YSZ/Gd-doped ceria (CGO) buffer layer/lanthanum strontium cobalt ferrite-samarium doped ceria (LSCF-SDC)), impregnated with catalyst was designed; this novel SOFC was then examined for operation at a low SSCR value of the autothermal reformer conditions (near maximum efficiency of n-C₄H₁₀ reformer and thermal neutral point, SSCR = 0.5, OCR = 0.5 and SCR = 1.3). The voltage for the metal-foam supported SOFC impregnated with 0.5 wt% Rh/ CGO remained at a nearly constant value, around 0.8 V, for 200 h under a constant temperature of 750 °C and current load of 250 mA cm^-2.

A01	`01`	`1`		`@0 0360-3199`
A02	`01`			`@0 IJHEDX`
A03		`1`		`@0 Int. j. hydrogen energy`
A05				`@2 35`
A06				`@2 22`
A08	`01`	`1`	`ENG`	`@1 Performance of SOFC coupled with n-C₄H₁₀ autothermal reformer: Carbon deposition and development of anode structure`
A11	`01`	`1`		`@1 BAE (Gyujong)`
A11	`02`	`1`		`@1 BAE (Joongmyeon)`
A11	`03`	`1`		`@1 KIM-LOHSOONTORN (Pattaraporn)`
A11	`04`	`1`		`@1 JEONG (Jihoon)`
A14	`01`			`@1 Department of Mechanical Engineering, Korea Advance Institute of Science and Technology (KAIST) @2 Daejeon 305-701 @3 KOR @Z 1 aut. @Z 2 aut. @Z 4 aut.`
A14	`02`			`@1 KI for Eco-Energy, Korea Advance Institute of Science and Technology (KAIST), Guseong-dong @2 Yuseong-gu, Daejeon 305-701 @3 KOR @Z 2 aut. @Z 3 aut.`
A14	`03`			`@1 Department of Chemical Engineering, Mahidol University @2 Nakorn Pathom 73170 @3 THA @Z 3 aut.`
A20				`@1 12346-12358`
A21				`@1 2010`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 17522 @5 354000193431450230`
A44				`@0 0000 @1 © 2011 INIST-CNRS. All rights reserved.`
A45				`@0 34 ref.`
A47	`01`	`1`		`@0 11-0087936`
A60				`@1 P`
A61				`@0 A`
A64	`01`	`1`		`@0 International journal of hydrogen energy`
A66	`01`			`@0 GBR`
C01	`01`		`ENG`	@0 The performance deterioration of solid oxide fuel cells (SOFCs, Nickel-Yttria stabilized zirconia (Ni-YSZ)/YSZ/lanthanum doped strontium manganite-YSZ (LSM-YSZ)) coupled with n-C₄H₁₀ steam reformers (SR), autothermal reformers (ATR), or catalytic partial oxidation reformers (CPOX) was examined using an integrated system of a micro-reactor reformer and SOFC unit. The terminal voltage rapidly degraded in CPOX-driven SOFC (oxygen to carbon ratio (OCR) = 0.5) while it was fairly stable for SR-driven SOFC (steam to carbon ratio (SCR) = 2) over 250 h. For ATR-driven SOFC at near the thermoneutral point (OCR = 0.5 and steam to carbon ration (SCR) = 1.3), significant deterioration of the terminal voltage was observed in 100 h of operation. The main precursors of carbon deposition on the SOFC were identified by reformate gas analysis during the tests. In this study, we reveal that the carbon deposition on the SOFC anode can be affected by not only lower-order hydrocarbons (C₁C₄), but also by the CO/H₂ gas mixture. The change in electrical conductivity of the Ni-YSZ cermet used for the SOFC anode was investigated under different gas mixtures. To investigate the propensity for carbon deposition by each carbon-containing gas mixture, we defined the ratios of steam to specific carbon (C₁C₄ lower-order hydrocarbons and CO) in the reformate gas (SSCR, steam to specific carbon ratio). To inhibit carbon deposition on SOFC anode, the SSCR must be sufficiently high. However, the reformer operates near its maximum efficiency at low SSCR value and the higher the SSCR value, the lower the open circuit voltage and operating power density due to Nernst potential. In this study, a metal-foam supported SOFC single cell (Ni-YSZ/YSZ/Gd-doped ceria (CGO) buffer layer/lanthanum strontium cobalt ferrite-samarium doped ceria (LSCF-SDC)), impregnated with catalyst was designed; this novel SOFC was then examined for operation at a low SSCR value of the autothermal reformer conditions (near maximum efficiency of n-C₄H₁₀ reformer and thermal neutral point, SSCR = 0.5, OCR = 0.5 and SCR = 1.3). The voltage for the metal-foam supported SOFC impregnated with 0.5 wt% Rh/ CGO remained at a nearly constant value, around 0.8 V, for 200 h under a constant temperature of 750 °C and current load of 250 mA cm^-2.
C02	`01`	`X`		`@0 001D06B06B`
C02	`02`	`X`		`@0 230`
C03	`01`	`X`	`FRE`	`@0 Performance @5 05`
C03	`01`	`X`	`ENG`	`@0 Performance @5 05`
C03	`01`	`X`	`SPA`	`@0 Rendimiento @5 05`
C03	`02`	`X`	`FRE`	`@0 Pile combustible @5 06`
C03	`02`	`X`	`ENG`	`@0 Fuel cell @5 06`
C03	`02`	`X`	`SPA`	`@0 Pila combustión @5 06`
C03	`03`	`X`	`FRE`	`@0 Pile combustible oxyde solide @5 07`
C03	`03`	`X`	`ENG`	`@0 Solid oxide fuel cell @5 07`
C03	`03`	`X`	`SPA`	`@0 Pila combustible oxido sólido @5 07`
C03	`04`	`X`	`FRE`	`@0 Anode @5 08`
C03	`04`	`X`	`ENG`	`@0 Anode @5 08`
C03	`04`	`X`	`SPA`	`@0 Anodo @5 08`
C03	`05`	`X`	`FRE`	`@0 Nickel @2 NC @2 FX @5 09`
C03	`05`	`X`	`ENG`	`@0 Nickel @2 NC @2 FX @5 09`
C03	`05`	`X`	`SPA`	`@0 Niquel @2 NC @2 FX @5 09`
C03	`06`	`X`	`FRE`	`@0 Zircone @5 10`
C03	`06`	`X`	`ENG`	`@0 Zirconia @5 10`
C03	`06`	`X`	`SPA`	`@0 Zircona @5 10`
C03	`07`	`X`	`FRE`	`@0 Oxyde de zirconium @5 11`
C03	`07`	`X`	`ENG`	`@0 Zirconium oxide @5 11`
C03	`07`	`X`	`SPA`	`@0 Zirconio óxido @5 11`
C03	`08`	`X`	`FRE`	`@0 Lanthane @2 NC @5 12`
C03	`08`	`X`	`ENG`	`@0 Lanthanum @2 NC @5 12`
C03	`08`	`X`	`SPA`	`@0 Lantano @2 NC @5 12`
C03	`09`	`X`	`FRE`	`@0 Reformage vapeur @5 13`
C03	`09`	`X`	`ENG`	`@0 Steam reforming @5 13`
C03	`09`	`X`	`SPA`	`@0 Reformación vapor @5 13`
C03	`10`	`X`	`FRE`	`@0 Oxydation partielle @5 14`
C03	`10`	`X`	`ENG`	`@0 Partial oxidation @5 14`
C03	`10`	`X`	`SPA`	`@0 Oxidación parcial @5 14`
C03	`11`	`X`	`FRE`	`@0 Vapeur eau @5 15`
C03	`11`	`X`	`ENG`	`@0 Water vapor @5 15`
C03	`11`	`X`	`SPA`	`@0 Vapor agua @5 15`
C03	`12`	`X`	`FRE`	`@0 Hydrocarbure @2 FX @5 16`
C03	`12`	`X`	`ENG`	`@0 Hydrocarbon @2 FX @5 16`
C03	`12`	`X`	`SPA`	`@0 Hidrocarburo @2 FX @5 16`
C03	`13`	`X`	`FRE`	`@0 Mélange gaz @5 17`
C03	`13`	`X`	`ENG`	`@0 Gas mixture @5 17`
C03	`13`	`X`	`SPA`	`@0 Mezcla gas @5 17`
C03	`14`	`X`	`FRE`	`@0 Conductivité électrique @5 18`
C03	`14`	`X`	`ENG`	`@0 Electrical conductivity @5 18`
C03	`14`	`X`	`SPA`	`@0 Conductividad eléctrica @5 18`
C03	`15`	`X`	`FRE`	`@0 Oxyde de cérium @5 19`
C03	`15`	`X`	`ENG`	`@0 Cerium oxide @5 19`
C03	`15`	`X`	`SPA`	`@0 Cerio óxido @5 19`
C03	`16`	`X`	`FRE`	`@0 Cobalt @2 NC @5 20`
C03	`16`	`X`	`ENG`	`@0 Cobalt @2 NC @5 20`
C03	`16`	`X`	`SPA`	`@0 Cobalto @2 NC @5 20`
C03	`17`	`X`	`FRE`	`@0 Ferrite @5 21`
C03	`17`	`X`	`ENG`	`@0 Ferrite @5 21`
C03	`17`	`X`	`SPA`	`@0 Ferrita @5 21`
C03	`18`	`X`	`FRE`	`@0 Samarium @2 NC @5 22`
C03	`18`	`X`	`ENG`	`@0 Samarium @2 NC @5 22`
C03	`18`	`X`	`SPA`	`@0 Samario @2 NC @5 22`
C03	`19`	`X`	`FRE`	`@0 Catalyseur @5 23`
C03	`19`	`X`	`ENG`	`@0 Catalyst @5 23`
C03	`19`	`X`	`SPA`	`@0 Catalizador @5 23`
C03	`20`	`X`	`FRE`	`@0 Rhodium @2 NC @5 24`
C03	`20`	`X`	`ENG`	`@0 Rhodium @2 NC @5 24`
C03	`20`	`X`	`SPA`	`@0 Rodio @2 NC @5 24`
C03	`21`	`3`	`FRE`	`@0 Processus reformage autothermique @5 25`
C03	`21`	`3`	`ENG`	`@0 Autothermal reformer processes @5 25`
C03	`22`	`X`	`FRE`	`@0 Hydrogène @2 NC @5 26`
C03	`22`	`X`	`ENG`	`@0 Hydrogen @2 NC @5 26`
C03	`22`	`X`	`SPA`	`@0 Hidrógeno @2 NC @5 26`
N21				`@1 059`
N44	`01`			`@1 OTO`
N82				`@1 OTO`

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Pascal:11-0087936

Le document en format XML

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<author><name sortKey="Kim Lohsoontorn, Pattaraporn" sort="Kim Lohsoontorn, Pattaraporn" uniqKey="Kim Lohsoontorn P" first="Pattaraporn" last="Kim-Lohsoontorn">Pattaraporn Kim-Lohsoontorn</name>
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<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Anode</term>
<term>Autothermal reformer processes</term>
<term>Catalyst</term>
<term>Cerium oxide</term>
<term>Cobalt</term>
<term>Electrical conductivity</term>
<term>Ferrite</term>
<term>Fuel cell</term>
<term>Gas mixture</term>
<term>Hydrocarbon</term>
<term>Hydrogen</term>
<term>Lanthanum</term>
<term>Nickel</term>
<term>Partial oxidation</term>
<term>Performance</term>
<term>Rhodium</term>
<term>Samarium</term>
<term>Solid oxide fuel cell</term>
<term>Steam reforming</term>
<term>Water vapor</term>
<term>Zirconia</term>
<term>Zirconium oxide</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Performance</term>
<term>Pile combustible</term>
<term>Pile combustible oxyde solide</term>
<term>Anode</term>
<term>Nickel</term>
<term>Zircone</term>
<term>Oxyde de zirconium</term>
<term>Lanthane</term>
<term>Reformage vapeur</term>
<term>Oxydation partielle</term>
<term>Vapeur eau</term>
<term>Hydrocarbure</term>
<term>Mélange gaz</term>
<term>Conductivité électrique</term>
<term>Oxyde de cérium</term>
<term>Cobalt</term>
<term>Ferrite</term>
<term>Samarium</term>
<term>Catalyseur</term>
<term>Rhodium</term>
<term>Processus reformage autothermique</term>
<term>Hydrogène</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Nickel</term>
<term>Hydrocarbure</term>
<term>Cobalt</term>
<term>Hydrogène</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front><div type="abstract" xml:lang="en">The performance deterioration of solid oxide fuel cells (SOFCs, Nickel-Yttria stabilized zirconia (Ni-YSZ)/YSZ/lanthanum doped strontium manganite-YSZ (LSM-YSZ)) coupled with n-C<sub>4</sub>
H<sub>10</sub>
 steam reformers (SR), autothermal reformers (ATR), or catalytic partial oxidation reformers (CPOX) was examined using an integrated system of a micro-reactor reformer and SOFC unit. The terminal voltage rapidly degraded in CPOX-driven SOFC (oxygen to carbon ratio (OCR) = 0.5) while it was fairly stable for SR-driven SOFC (steam to carbon ratio (SCR) = 2) over 250 h. For ATR-driven SOFC at near the thermoneutral point (OCR = 0.5 and steam to carbon ration (SCR) = 1.3), significant deterioration of the terminal voltage was observed in 100 h of operation. The main precursors of carbon deposition on the SOFC were identified by reformate gas analysis during the tests. In this study, we reveal that the carbon deposition on the SOFC anode can be affected by not only lower-order hydrocarbons (C<sub>1</sub>
C<sub>4</sub>
), but also by the CO/H<sub>2</sub>
 gas mixture. The change in electrical conductivity of the Ni-YSZ cermet used for the SOFC anode was investigated under different gas mixtures. To investigate the propensity for carbon deposition by each carbon-containing gas mixture, we defined the ratios of steam to specific carbon (C<sub>1</sub>
C<sub>4</sub>
 lower-order hydrocarbons and CO) in the reformate gas (SSCR, steam to specific carbon ratio). To inhibit carbon deposition on SOFC anode, the SSCR must be sufficiently high. However, the reformer operates near its maximum efficiency at low SSCR value and the higher the SSCR value, the lower the open circuit voltage and operating power density due to Nernst potential. In this study, a metal-foam supported SOFC single cell (Ni-YSZ/YSZ/Gd-doped ceria (CGO) buffer layer/lanthanum strontium cobalt ferrite-samarium doped ceria (LSCF-SDC)), impregnated with catalyst was designed; this novel SOFC was then examined for operation at a low SSCR value of the autothermal reformer conditions (near maximum efficiency of n-C<sub>4</sub>
H<sub>10</sub>
 reformer and thermal neutral point, SSCR = 0.5, OCR = 0.5 and SCR = 1.3). The voltage for the metal-foam supported SOFC impregnated with 0.5 wt% Rh/ CGO remained at a nearly constant value, around 0.8 V, for 200 h under a constant temperature of 750 °C and current load of 250 mA cm<sup>-2</sup>
.</div>
</front>
</TEI>
<inist><standard h6="B"><pA><fA01 i1="01" i2="1"><s0>0360-3199</s0>
</fA01>
<fA02 i1="01"><s0>IJHEDX</s0>
</fA02>
<fA03 i2="1"><s0>Int. j. hydrogen energy</s0>
</fA03>
<fA05><s2>35</s2>
</fA05>
<fA06><s2>22</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Performance of SOFC coupled with n-C<sub>4</sub>
H<sub>10</sub>
 autothermal reformer: Carbon deposition and development of anode structure</s1>
</fA08>
<fA11 i1="01" i2="1"><s1>BAE (Gyujong)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>BAE (Joongmyeon)</s1>
</fA11>
<fA11 i1="03" i2="1"><s1>KIM-LOHSOONTORN (Pattaraporn)</s1>
</fA11>
<fA11 i1="04" i2="1"><s1>JEONG (Jihoon)</s1>
</fA11>
<fA14 i1="01"><s1>Department of Mechanical Engineering, Korea Advance Institute of Science and Technology (KAIST)</s1>
<s2>Daejeon 305-701</s2>
<s3>KOR</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
<sZ>4 aut.</sZ>
</fA14>
<fA14 i1="02"><s1>KI for Eco-Energy, Korea Advance Institute of Science and Technology (KAIST), Guseong-dong</s1>
<s2>Yuseong-gu, Daejeon 305-701</s2>
<s3>KOR</s3>
<sZ>2 aut.</sZ>
<sZ>3 aut.</sZ>
</fA14>
<fA14 i1="03"><s1>Department of Chemical Engineering, Mahidol University</s1>
<s2>Nakorn Pathom 73170</s2>
<s3>THA</s3>
<sZ>3 aut.</sZ>
</fA14>
<fA20><s1>12346-12358</s1>
</fA20>
<fA21><s1>2010</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>17522</s2>
<s5>354000193431450230</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2011 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>34 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>11-0087936</s0>
</fA47>
<fA60><s1>P</s1>
</fA60>
<fA61><s0>A</s0>
</fA61>
<fA64 i1="01" i2="1"><s0>International journal of hydrogen energy</s0>
</fA64>
<fA66 i1="01"><s0>GBR</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>The performance deterioration of solid oxide fuel cells (SOFCs, Nickel-Yttria stabilized zirconia (Ni-YSZ)/YSZ/lanthanum doped strontium manganite-YSZ (LSM-YSZ)) coupled with n-C<sub>4</sub>
H<sub>10</sub>
 steam reformers (SR), autothermal reformers (ATR), or catalytic partial oxidation reformers (CPOX) was examined using an integrated system of a micro-reactor reformer and SOFC unit. The terminal voltage rapidly degraded in CPOX-driven SOFC (oxygen to carbon ratio (OCR) = 0.5) while it was fairly stable for SR-driven SOFC (steam to carbon ratio (SCR) = 2) over 250 h. For ATR-driven SOFC at near the thermoneutral point (OCR = 0.5 and steam to carbon ration (SCR) = 1.3), significant deterioration of the terminal voltage was observed in 100 h of operation. The main precursors of carbon deposition on the SOFC were identified by reformate gas analysis during the tests. In this study, we reveal that the carbon deposition on the SOFC anode can be affected by not only lower-order hydrocarbons (C<sub>1</sub>
C<sub>4</sub>
), but also by the CO/H<sub>2</sub>
 gas mixture. The change in electrical conductivity of the Ni-YSZ cermet used for the SOFC anode was investigated under different gas mixtures. To investigate the propensity for carbon deposition by each carbon-containing gas mixture, we defined the ratios of steam to specific carbon (C<sub>1</sub>
C<sub>4</sub>
 lower-order hydrocarbons and CO) in the reformate gas (SSCR, steam to specific carbon ratio). To inhibit carbon deposition on SOFC anode, the SSCR must be sufficiently high. However, the reformer operates near its maximum efficiency at low SSCR value and the higher the SSCR value, the lower the open circuit voltage and operating power density due to Nernst potential. In this study, a metal-foam supported SOFC single cell (Ni-YSZ/YSZ/Gd-doped ceria (CGO) buffer layer/lanthanum strontium cobalt ferrite-samarium doped ceria (LSCF-SDC)), impregnated with catalyst was designed; this novel SOFC was then examined for operation at a low SSCR value of the autothermal reformer conditions (near maximum efficiency of n-C<sub>4</sub>
H<sub>10</sub>
 reformer and thermal neutral point, SSCR = 0.5, OCR = 0.5 and SCR = 1.3). The voltage for the metal-foam supported SOFC impregnated with 0.5 wt% Rh/ CGO remained at a nearly constant value, around 0.8 V, for 200 h under a constant temperature of 750 °C and current load of 250 mA cm<sup>-2</sup>
.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001D06B06B</s0>
</fC02>
<fC02 i1="02" i2="X"><s0>230</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Performance</s0>
<s5>05</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Performance</s0>
<s5>05</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Rendimiento</s0>
<s5>05</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Pile combustible</s0>
<s5>06</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Fuel cell</s0>
<s5>06</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Pila combustión</s0>
<s5>06</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Pile combustible oxyde solide</s0>
<s5>07</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Solid oxide fuel cell</s0>
<s5>07</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Pila combustible oxido sólido</s0>
<s5>07</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Anode</s0>
<s5>08</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Anode</s0>
<s5>08</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Anodo</s0>
<s5>08</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>09</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>09</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Niquel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>09</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Zircone</s0>
<s5>10</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Zirconia</s0>
<s5>10</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Zircona</s0>
<s5>10</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Oxyde de zirconium</s0>
<s5>11</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Zirconium oxide</s0>
<s5>11</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Zirconio óxido</s0>
<s5>11</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Lanthane</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Lanthanum</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Lantano</s0>
<s2>NC</s2>
<s5>12</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Reformage vapeur</s0>
<s5>13</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Steam reforming</s0>
<s5>13</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Reformación vapor</s0>
<s5>13</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Oxydation partielle</s0>
<s5>14</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Partial oxidation</s0>
<s5>14</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Oxidación parcial</s0>
<s5>14</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Vapeur eau</s0>
<s5>15</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Water vapor</s0>
<s5>15</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Vapor agua</s0>
<s5>15</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>16</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>16</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>16</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Mélange gaz</s0>
<s5>17</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Gas mixture</s0>
<s5>17</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Mezcla gas</s0>
<s5>17</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Conductivité électrique</s0>
<s5>18</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Electrical conductivity</s0>
<s5>18</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Conductividad eléctrica</s0>
<s5>18</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Oxyde de cérium</s0>
<s5>19</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Cerium oxide</s0>
<s5>19</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Cerio óxido</s0>
<s5>19</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Cobalt</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Cobalt</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Cobalto</s0>
<s2>NC</s2>
<s5>20</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Ferrite</s0>
<s5>21</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Ferrite</s0>
<s5>21</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Ferrita</s0>
<s5>21</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Samarium</s0>
<s2>NC</s2>
<s5>22</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>Samarium</s0>
<s2>NC</s2>
<s5>22</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Samario</s0>
<s2>NC</s2>
<s5>22</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Catalyseur</s0>
<s5>23</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Catalyst</s0>
<s5>23</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Catalizador</s0>
<s5>23</s5>
</fC03>
<fC03 i1="20" i2="X" l="FRE"><s0>Rhodium</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="20" i2="X" l="ENG"><s0>Rhodium</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="20" i2="X" l="SPA"><s0>Rodio</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="21" i2="3" l="FRE"><s0>Processus reformage autothermique</s0>
<s5>25</s5>
</fC03>
<fC03 i1="21" i2="3" l="ENG"><s0>Autothermal reformer processes</s0>
<s5>25</s5>
</fC03>
<fC03 i1="22" i2="X" l="FRE"><s0>Hydrogène</s0>
<s2>NC</s2>
<s5>26</s5>
</fC03>
<fC03 i1="22" i2="X" l="ENG"><s0>Hydrogen</s0>
<s2>NC</s2>
<s5>26</s5>
</fC03>
<fC03 i1="22" i2="X" l="SPA"><s0>Hidrógeno</s0>
<s2>NC</s2>
<s5>26</s5>
</fC03>
<fN21><s1>059</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
</fN44>
<fN82><s1>OTO</s1>
</fN82>
</pA>
</standard>
</inist>
</record>

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Performance of SOFC coupled with n-C4H10 autothermal reformer: Carbon deposition and development of anode structure

Performance of SOFC coupled with n-C4H10 autothermal reformer: Carbon deposition and development of anode structure

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