Standard

Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes. / Popov, Mikhail P.; Maslennikov, Daniel V.; Gainutdinov, Igor I. и др.

в: Catalysis Today, Том 329, 01.06.2019, стр. 167-170.

Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование

Harvard

Popov, MP, Maslennikov, DV, Gainutdinov, II, Gulyaev, IP, Zagoruiko, AN & Nemudry, AP 2019, 'Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes', Catalysis Today, Том. 329, стр. 167-170. https://doi.org/10.1016/j.cattod.2018.11.009

APA

Popov, M. P., Maslennikov, D. V., Gainutdinov, I. I., Gulyaev, I. P., Zagoruiko, A. N., & Nemudry, A. P. (2019). Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes. Catalysis Today, 329, 167-170. https://doi.org/10.1016/j.cattod.2018.11.009

Vancouver

Popov MP, Maslennikov DV, Gainutdinov II, Gulyaev IP, Zagoruiko AN, Nemudry AP. Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes. Catalysis Today. 2019 июнь 1;329:167-170. doi: 10.1016/j.cattod.2018.11.009

Author

Popov, Mikhail P. ; Maslennikov, Daniel V. ; Gainutdinov, Igor I. и др. / Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes. в: Catalysis Today. 2019 ; Том 329. стр. 167-170.

BibTeX

@article{19e4fc5870134d40b2a66db4cd04e11a,
title = "Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes",
abstract = "AC heated oxygen-permeable microtubular membranes with the composition Ba0.5Sr0.5Co0.78W0.02Fe0.2O3- δ were used to provide catalytic reforming of methane into C2- hydrocarbons. The methane conversion degree about 60% and acetylene yield about 27% at 1200 °C was achieved. Microtubular solid oxide fuel cells based on gadolinium-doped ceria with perovskite-like cathode material composed of Ba0.5Sr0.5Co0.75Mo0.05Fe0.2O3- δ were prepared. The MT-SOFC demonstrates maximum power densities of 50, 100, 200 mW/cm2 at 550, 600, 650 °C, respectively with humidified H2 as fuel and ambient air as oxidant.",
keywords = "Catalytic reforming, Dip-coating, Microtubular solid oxide fuel cell (MT-SOFC), Oxygen-permeable membranes, Phase inversion, OXYGEN PERMEATION",
author = "Popov, {Mikhail P.} and Maslennikov, {Daniel V.} and Gainutdinov, {Igor I.} and Gulyaev, {Igor P.} and Zagoruiko, {Andrey N.} and Nemudry, {Alexander P.}",
year = "2019",
month = jun,
day = "1",
doi = "10.1016/j.cattod.2018.11.009",
language = "English",
volume = "329",
pages = "167--170",
journal = "Catalysis Today",
issn = "0920-5861",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - Compact solid oxide fuel cells and catalytic reformers based on microtubular membranes

AU - Popov, Mikhail P.

AU - Maslennikov, Daniel V.

AU - Gainutdinov, Igor I.

AU - Gulyaev, Igor P.

AU - Zagoruiko, Andrey N.

AU - Nemudry, Alexander P.

PY - 2019/6/1

Y1 - 2019/6/1

N2 - AC heated oxygen-permeable microtubular membranes with the composition Ba0.5Sr0.5Co0.78W0.02Fe0.2O3- δ were used to provide catalytic reforming of methane into C2- hydrocarbons. The methane conversion degree about 60% and acetylene yield about 27% at 1200 °C was achieved. Microtubular solid oxide fuel cells based on gadolinium-doped ceria with perovskite-like cathode material composed of Ba0.5Sr0.5Co0.75Mo0.05Fe0.2O3- δ were prepared. The MT-SOFC demonstrates maximum power densities of 50, 100, 200 mW/cm2 at 550, 600, 650 °C, respectively with humidified H2 as fuel and ambient air as oxidant.

AB - AC heated oxygen-permeable microtubular membranes with the composition Ba0.5Sr0.5Co0.78W0.02Fe0.2O3- δ were used to provide catalytic reforming of methane into C2- hydrocarbons. The methane conversion degree about 60% and acetylene yield about 27% at 1200 °C was achieved. Microtubular solid oxide fuel cells based on gadolinium-doped ceria with perovskite-like cathode material composed of Ba0.5Sr0.5Co0.75Mo0.05Fe0.2O3- δ were prepared. The MT-SOFC demonstrates maximum power densities of 50, 100, 200 mW/cm2 at 550, 600, 650 °C, respectively with humidified H2 as fuel and ambient air as oxidant.

KW - Catalytic reforming

KW - Dip-coating

KW - Microtubular solid oxide fuel cell (MT-SOFC)

KW - Oxygen-permeable membranes

KW - Phase inversion

KW - OXYGEN PERMEATION

UR - http://www.scopus.com/inward/record.url?scp=85057247985&partnerID=8YFLogxK

U2 - 10.1016/j.cattod.2018.11.009

DO - 10.1016/j.cattod.2018.11.009

M3 - Article

AN - SCOPUS:85057247985

VL - 329

SP - 167

EP - 170

JO - Catalysis Today

JF - Catalysis Today

SN - 0920-5861

ER -

ID: 17553433