Standard

Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst. / Makarshin, L. L.; Sadykov, V. A.; Andreev, D. V. et al.

In: Fuel Processing Technology, Vol. 131, 03.2015, p. 21-28.

Research output: Contribution to journal › Article › peer-review

Harvard

Makarshin, LL, Sadykov, VA, Andreev, DV, Gribovskii, AG, Privezentsev, VV & Parmon, VN 2015, 'Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst', Fuel Processing Technology, vol. 131, pp. 21-28. https://doi.org/10.1016/j.fuproc.2014.10.031

APA

Makarshin, L. L., Sadykov, V. A., Andreev, D. V., Gribovskii, A. G., Privezentsev, V. V., & Parmon, V. N. (2015). Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst. Fuel Processing Technology, 131, 21-28. https://doi.org/10.1016/j.fuproc.2014.10.031

Vancouver

Makarshin LL, Sadykov VA, Andreev DV, Gribovskii AG, Privezentsev VV, Parmon VN. Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst. Fuel Processing Technology. 2015 Mar;131:21-28. doi: 10.1016/j.fuproc.2014.10.031

Author

Makarshin, L. L. ; Sadykov, V. A. ; Andreev, D. V. et al. / Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst. In: Fuel Processing Technology. 2015 ; Vol. 131. pp. 21-28.

BibTeX

@article{457a2167c334494482906020223aa94a,
title = "Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst",
abstract = "Operation of a microchannel reactor during the partial oxidation of methane has been studied. Methods for the deposition of a durable (Ni-Pt)/LaCeZrO catalyst on the Fecralloy microchannel plates working under thermocycling (up to 900 °C) conditions up were developed. It was shown that the temperature profile along the microchannel plate length is not flat. A part of methane is combusted into H2O and CO2 at the front edge of the microchannel plate, which is accompanied by a big heat release. On the rest part of the microchannel plate, endothermic reactions of methane steam and dry reforming occur yielding CO and H2. As a result, the front edge of the microchannel plate (up to 2 mm in length) undergoes a heavy thermal corrosion. Test runs of the microchannel reactor with one microchannel plate demonstrated 82% methane conversion and 60% selectivity toward carbon monoxide at gas space velocity of 820,000 h-1. Scaling of the MC reactor increased hydrogen production proportionally to the number of the MC plates. The specific hydrogen production related to the volume occupied by the MC plates is about 123 L/(h·cm3).",
keywords = "Hydrogen production, Methane, Microchannel plate, Microchannel reactor, Partial oxidation, Syngas",
author = "Makarshin, {L. L.} and Sadykov, {V. A.} and Andreev, {D. V.} and Gribovskii, {A. G.} and Privezentsev, {V. V.} and Parmon, {V. N.}",
year = "2015",
month = mar,
doi = "10.1016/j.fuproc.2014.10.031",
language = "English",
volume = "131",
pages = "21--28",
journal = "Fuel Processing Technology",
issn = "0378-3820",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - Syngas production by partial oxidation of methane in a microchannel reactor over a Ni-Pt/La0.2Zr0.4Ce0.4Ox catalyst

AU - Makarshin, L. L.

AU - Sadykov, V. A.

AU - Andreev, D. V.

AU - Gribovskii, A. G.

AU - Privezentsev, V. V.

AU - Parmon, V. N.

PY - 2015/3

Y1 - 2015/3

N2 - Operation of a microchannel reactor during the partial oxidation of methane has been studied. Methods for the deposition of a durable (Ni-Pt)/LaCeZrO catalyst on the Fecralloy microchannel plates working under thermocycling (up to 900 °C) conditions up were developed. It was shown that the temperature profile along the microchannel plate length is not flat. A part of methane is combusted into H2O and CO2 at the front edge of the microchannel plate, which is accompanied by a big heat release. On the rest part of the microchannel plate, endothermic reactions of methane steam and dry reforming occur yielding CO and H2. As a result, the front edge of the microchannel plate (up to 2 mm in length) undergoes a heavy thermal corrosion. Test runs of the microchannel reactor with one microchannel plate demonstrated 82% methane conversion and 60% selectivity toward carbon monoxide at gas space velocity of 820,000 h-1. Scaling of the MC reactor increased hydrogen production proportionally to the number of the MC plates. The specific hydrogen production related to the volume occupied by the MC plates is about 123 L/(h·cm3).

AB - Operation of a microchannel reactor during the partial oxidation of methane has been studied. Methods for the deposition of a durable (Ni-Pt)/LaCeZrO catalyst on the Fecralloy microchannel plates working under thermocycling (up to 900 °C) conditions up were developed. It was shown that the temperature profile along the microchannel plate length is not flat. A part of methane is combusted into H2O and CO2 at the front edge of the microchannel plate, which is accompanied by a big heat release. On the rest part of the microchannel plate, endothermic reactions of methane steam and dry reforming occur yielding CO and H2. As a result, the front edge of the microchannel plate (up to 2 mm in length) undergoes a heavy thermal corrosion. Test runs of the microchannel reactor with one microchannel plate demonstrated 82% methane conversion and 60% selectivity toward carbon monoxide at gas space velocity of 820,000 h-1. Scaling of the MC reactor increased hydrogen production proportionally to the number of the MC plates. The specific hydrogen production related to the volume occupied by the MC plates is about 123 L/(h·cm3).

KW - Hydrogen production

KW - Methane

KW - Microchannel plate

KW - Microchannel reactor

KW - Partial oxidation

KW - Syngas

UR - http://www.scopus.com/inward/record.url?scp=84923336907&partnerID=8YFLogxK

U2 - 10.1016/j.fuproc.2014.10.031

DO - 10.1016/j.fuproc.2014.10.031

M3 - Article

AN - SCOPUS:84923336907

VL - 131

SP - 21

EP - 28

JO - Fuel Processing Technology

JF - Fuel Processing Technology

SN - 0378-3820

ER -

ID: 25397151