Standard

Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production. / Lysikov, Anton; Derevschikov, Vladimir; Okunev, Alexey.

в: International Journal of Hydrogen Energy, Том 40, № 42, 2015, стр. 14436-14444.

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

Harvard

Lysikov, A, Derevschikov, V & Okunev, A 2015, 'Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production', International Journal of Hydrogen Energy, Том. 40, № 42, стр. 14436-14444. https://doi.org/10.1016/j.ijhydene.2015.06.029

APA

Lysikov, A., Derevschikov, V., & Okunev, A. (2015). Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production. International Journal of Hydrogen Energy, 40(42), 14436-14444. https://doi.org/10.1016/j.ijhydene.2015.06.029

Vancouver

Lysikov A, Derevschikov V, Okunev A. Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production. International Journal of Hydrogen Energy. 2015;40(42):14436-14444. doi: 10.1016/j.ijhydene.2015.06.029

Author

Lysikov, Anton ; Derevschikov, Vladimir ; Okunev, Alexey. / Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production. в: International Journal of Hydrogen Energy. 2015 ; Том 40, № 42. стр. 14436-14444.

BibTeX

@article{d507dded384a4207bf9ab9625f25b131,
title = "Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production",
abstract = "The sorption enhanced reforming (SER) of ethanol over an admixture of CaO sorbent and Ni reforming catalyst has been experimentally studied in a periodically operated dual fixed bed reactor. The optimal parameters for SER process were calculated from thermodynamic data. The experiment was carried out in cyclic mode; temperature swing adsorption and pressure swing adsorption (PSA) modes were used for periodic sorbent regeneration. It was shown that the continuous hydrogen production and the purity of hydrogen during the sorption-catalytic ethanol reforming maintained at the constant level and were 50 L/min and 97e99 vol.% respectively. The dual fixed bed SER reactor worked fine during 2 months on stream and more than 250 cycles. Both the sorbent and the catalyst maintained the sufficient activity during experiment. The obtained results suggest that sorption enhanced reforming may be a perspective approach for hydrogen production in fuel cell powered cogeneration systems.",
keywords = "Adsorption, Carbon dioxide sorbent, High temperature pressure swing, Hydrogen production, Sorption-enhanced reforming",
author = "Anton Lysikov and Vladimir Derevschikov and Alexey Okunev",
year = "2015",
doi = "10.1016/j.ijhydene.2015.06.029",
language = "English",
volume = "40",
pages = "14436--14444",
journal = "International Journal of Hydrogen Energy",
issn = "0360-3199",
publisher = "Elsevier Ltd",
number = "42",

}

RIS

TY - JOUR

T1 - Sorption-enhanced reforming of bioethanol in dual fixed bed reactor for continuous hydrogen production

AU - Lysikov, Anton

AU - Derevschikov, Vladimir

AU - Okunev, Alexey

PY - 2015

Y1 - 2015

N2 - The sorption enhanced reforming (SER) of ethanol over an admixture of CaO sorbent and Ni reforming catalyst has been experimentally studied in a periodically operated dual fixed bed reactor. The optimal parameters for SER process were calculated from thermodynamic data. The experiment was carried out in cyclic mode; temperature swing adsorption and pressure swing adsorption (PSA) modes were used for periodic sorbent regeneration. It was shown that the continuous hydrogen production and the purity of hydrogen during the sorption-catalytic ethanol reforming maintained at the constant level and were 50 L/min and 97e99 vol.% respectively. The dual fixed bed SER reactor worked fine during 2 months on stream and more than 250 cycles. Both the sorbent and the catalyst maintained the sufficient activity during experiment. The obtained results suggest that sorption enhanced reforming may be a perspective approach for hydrogen production in fuel cell powered cogeneration systems.

AB - The sorption enhanced reforming (SER) of ethanol over an admixture of CaO sorbent and Ni reforming catalyst has been experimentally studied in a periodically operated dual fixed bed reactor. The optimal parameters for SER process were calculated from thermodynamic data. The experiment was carried out in cyclic mode; temperature swing adsorption and pressure swing adsorption (PSA) modes were used for periodic sorbent regeneration. It was shown that the continuous hydrogen production and the purity of hydrogen during the sorption-catalytic ethanol reforming maintained at the constant level and were 50 L/min and 97e99 vol.% respectively. The dual fixed bed SER reactor worked fine during 2 months on stream and more than 250 cycles. Both the sorbent and the catalyst maintained the sufficient activity during experiment. The obtained results suggest that sorption enhanced reforming may be a perspective approach for hydrogen production in fuel cell powered cogeneration systems.

KW - Adsorption

KW - Carbon dioxide sorbent

KW - High temperature pressure swing

KW - Hydrogen production

KW - Sorption-enhanced reforming

UR - http://www.scopus.com/inward/record.url?scp=84948710231&partnerID=8YFLogxK

U2 - 10.1016/j.ijhydene.2015.06.029

DO - 10.1016/j.ijhydene.2015.06.029

M3 - Article

AN - SCOPUS:84948710231

VL - 40

SP - 14436

EP - 14444

JO - International Journal of Hydrogen Energy

JF - International Journal of Hydrogen Energy

SN - 0360-3199

IS - 42

ER -

ID: 8716298