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Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts. / Skrypnik, Andrey S.; Petrov, Sergey A.; Kondratenko, Vita A. et al.

In: ACS Catalysis, Vol. 12, No. 18, 16.09.2022, p. 11355-11368.

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

Harvard

Skrypnik, AS, Petrov, SA, Kondratenko, VA, Yang, Q, Lund, H, Matvienko, AA & Kondratenko, EV 2022, 'Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts', ACS Catalysis, vol. 12, no. 18, pp. 11355-11368. https://doi.org/10.1021/acscatal.2c03375

APA

Skrypnik, A. S., Petrov, S. A., Kondratenko, V. A., Yang, Q., Lund, H., Matvienko, A. A., & Kondratenko, E. V. (2022). Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts. ACS Catalysis, 12(18), 11355-11368. https://doi.org/10.1021/acscatal.2c03375

Vancouver

Skrypnik AS, Petrov SA, Kondratenko VA, Yang Q, Lund H, Matvienko AA et al. Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts. ACS Catalysis. 2022 Sept 16;12(18):11355-11368. doi: 10.1021/acscatal.2c03375

Author

Skrypnik, Andrey S. ; Petrov, Sergey A. ; Kondratenko, Vita A. et al. / Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts. In: ACS Catalysis. 2022 ; Vol. 12, No. 18. pp. 11355-11368.

BibTeX

@article{3194eee9bf0f44418c53b3b415ead389,
title = "Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts",
abstract = "Direct CO2 hydrogenation to higher hydrocarbons, that is, CO2 Fischer-Tropsch (CO2-FT) synthesis, is an attractive way to mitigate anthropogenic CO2 emissions and to produce fuels alternatively to oil- or natural-gas-based processes. One of the major shortcomings of typically applied Fe-based catalysts in CO2-FT is high selectivity to methane. Herein, we provide descriptors relevant for purposeful preparation of unpromoted Fe2O3 with the suppressed formation of this undesired product. This was possible owing to the combination of controlled material synthesis, sophisticated catalyst characterization (including along the catalyst bed) by state-of-the-art techniques with spatially resolved steady-state, and transient kinetic analyses. The defectiveness of in situ formed Fe5C2, that reflects the deviation from the stoichiometric composition and expressed as the ratio of C/Fe, affects the ability to adsorb CO2 and CO as well as to activate H2. CH4 formation is hindered over less-defective iron carbides, which are characterized by strong adsorption of CO and CO2 but low adsorption of H2. Thus, the catalyst efficiency in terms of C2+-hydrocarbon formation is improved. The imperfection of Fe5C2 can be controlled through the morphology of iron(II) oxalate dihydrate used as a precursor for preparation of Fe2O3. In addition to the defectiveness, the size of crystallites of α-Fe2O3 and the ratio of α-Fe2O3 to γFe2O3 in fresh samples are two indirect descriptors affecting the ability of in situ formed Fe5C2 to directly hydrogenate CO2 to CH4. These structural characteristics depend on temperature, at which Fe2O3 materials were prepared. The lowest achieved CH4 selectivity is 0.05 at CO2 conversion of about 0.2. The ratio of olefins to paraffins among C2-C4-hydrocarbons is about 6.",
keywords = "COFischer-Tropsch synthesis, COhydrogenation, ferrous oxalate decomposition, iron carbides, iron oxide, particle size effect, preparation method",
author = "Skrypnik, {Andrey S.} and Petrov, {Sergey A.} and Kondratenko, {Vita A.} and Qingxin Yang and Henrik Lund and Matvienko, {Alexander A.} and Kondratenko, {Evgenii V.}",
note = "Publisher Copyright: {\textcopyright} 2022 American Chemical Society.",
year = "2022",
month = sep,
day = "16",
doi = "10.1021/acscatal.2c03375",
language = "English",
volume = "12",
pages = "11355--11368",
journal = "ACS Catalysis",
issn = "2155-5435",
publisher = "American Chemical Society",
number = "18",

}

RIS

TY - JOUR

T1 - Descriptors Affecting Methane Selectivity in CO2Hydrogenation over Unpromoted Bulk Iron(III)-Based Catalysts

AU - Skrypnik, Andrey S.

AU - Petrov, Sergey A.

AU - Kondratenko, Vita A.

AU - Yang, Qingxin

AU - Lund, Henrik

AU - Matvienko, Alexander A.

AU - Kondratenko, Evgenii V.

N1 - Publisher Copyright: © 2022 American Chemical Society.

PY - 2022/9/16

Y1 - 2022/9/16

N2 - Direct CO2 hydrogenation to higher hydrocarbons, that is, CO2 Fischer-Tropsch (CO2-FT) synthesis, is an attractive way to mitigate anthropogenic CO2 emissions and to produce fuels alternatively to oil- or natural-gas-based processes. One of the major shortcomings of typically applied Fe-based catalysts in CO2-FT is high selectivity to methane. Herein, we provide descriptors relevant for purposeful preparation of unpromoted Fe2O3 with the suppressed formation of this undesired product. This was possible owing to the combination of controlled material synthesis, sophisticated catalyst characterization (including along the catalyst bed) by state-of-the-art techniques with spatially resolved steady-state, and transient kinetic analyses. The defectiveness of in situ formed Fe5C2, that reflects the deviation from the stoichiometric composition and expressed as the ratio of C/Fe, affects the ability to adsorb CO2 and CO as well as to activate H2. CH4 formation is hindered over less-defective iron carbides, which are characterized by strong adsorption of CO and CO2 but low adsorption of H2. Thus, the catalyst efficiency in terms of C2+-hydrocarbon formation is improved. The imperfection of Fe5C2 can be controlled through the morphology of iron(II) oxalate dihydrate used as a precursor for preparation of Fe2O3. In addition to the defectiveness, the size of crystallites of α-Fe2O3 and the ratio of α-Fe2O3 to γFe2O3 in fresh samples are two indirect descriptors affecting the ability of in situ formed Fe5C2 to directly hydrogenate CO2 to CH4. These structural characteristics depend on temperature, at which Fe2O3 materials were prepared. The lowest achieved CH4 selectivity is 0.05 at CO2 conversion of about 0.2. The ratio of olefins to paraffins among C2-C4-hydrocarbons is about 6.

AB - Direct CO2 hydrogenation to higher hydrocarbons, that is, CO2 Fischer-Tropsch (CO2-FT) synthesis, is an attractive way to mitigate anthropogenic CO2 emissions and to produce fuels alternatively to oil- or natural-gas-based processes. One of the major shortcomings of typically applied Fe-based catalysts in CO2-FT is high selectivity to methane. Herein, we provide descriptors relevant for purposeful preparation of unpromoted Fe2O3 with the suppressed formation of this undesired product. This was possible owing to the combination of controlled material synthesis, sophisticated catalyst characterization (including along the catalyst bed) by state-of-the-art techniques with spatially resolved steady-state, and transient kinetic analyses. The defectiveness of in situ formed Fe5C2, that reflects the deviation from the stoichiometric composition and expressed as the ratio of C/Fe, affects the ability to adsorb CO2 and CO as well as to activate H2. CH4 formation is hindered over less-defective iron carbides, which are characterized by strong adsorption of CO and CO2 but low adsorption of H2. Thus, the catalyst efficiency in terms of C2+-hydrocarbon formation is improved. The imperfection of Fe5C2 can be controlled through the morphology of iron(II) oxalate dihydrate used as a precursor for preparation of Fe2O3. In addition to the defectiveness, the size of crystallites of α-Fe2O3 and the ratio of α-Fe2O3 to γFe2O3 in fresh samples are two indirect descriptors affecting the ability of in situ formed Fe5C2 to directly hydrogenate CO2 to CH4. These structural characteristics depend on temperature, at which Fe2O3 materials were prepared. The lowest achieved CH4 selectivity is 0.05 at CO2 conversion of about 0.2. The ratio of olefins to paraffins among C2-C4-hydrocarbons is about 6.

KW - COFischer-Tropsch synthesis

KW - COhydrogenation

KW - ferrous oxalate decomposition

KW - iron carbides

KW - iron oxide

KW - particle size effect

KW - preparation method

UR - http://www.scopus.com/inward/record.url?scp=85137848461&partnerID=8YFLogxK

U2 - 10.1021/acscatal.2c03375

DO - 10.1021/acscatal.2c03375

M3 - Article

AN - SCOPUS:85137848461

VL - 12

SP - 11355

EP - 11368

JO - ACS Catalysis

JF - ACS Catalysis

SN - 2155-5435

IS - 18

ER -

ID: 38051383