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Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis

The production of linear alpha-olefins (α-olefins) is a practical way to increase the economic potential of the Fischer–Tropsch synthesis (FTS) because of their importance as chemical intermediates. Our study aimed to optimize Na-promoted Fe(1)Zn(1.2)O(x) catalysts such that they selectively convert...

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Autores principales: Yang, Sunkyu, Lee, Sungwoo, Kang, Seok Chang, Han, Seung Ju, Jun, Ki-Won, Lee, Kwan-Young, Kim, Yong Tae
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9064040/
https://www.ncbi.nlm.nih.gov/pubmed/35519344
http://dx.doi.org/10.1039/c9ra02471a
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author Yang, Sunkyu
Lee, Sungwoo
Kang, Seok Chang
Han, Seung Ju
Jun, Ki-Won
Lee, Kwan-Young
Kim, Yong Tae
author_facet Yang, Sunkyu
Lee, Sungwoo
Kang, Seok Chang
Han, Seung Ju
Jun, Ki-Won
Lee, Kwan-Young
Kim, Yong Tae
author_sort Yang, Sunkyu
collection PubMed
description The production of linear alpha-olefins (α-olefins) is a practical way to increase the economic potential of the Fischer–Tropsch synthesis (FTS) because of their importance as chemical intermediates. Our study aimed to optimize Na-promoted Fe(1)Zn(1.2)O(x) catalysts such that they selectively converted syngas to linear α-olefins via FTS at 340 °C and 2.0 MPa. The Fe(1)Zn(1.2)O(x) catalysts were calcined at different temperatures from 350 to 700 °C before Na anchoring. The increase in the size of the ZnFe(2)O(4) crystals comprising the catalyst had a negative effect on the reducibility of Fe oxides and the particle size of Fe(5)C(2) during the reaction. The Na species in the catalyst restrained the reduction of Fe(1)Zn(1.2)O(x) but facilitated the formation of Fe(5)C(2). When pure Fe(1)Zn(1.2)O(x) was calcined at 400 °C, the corresponding catalyst (i.e., Na(0.2)/Fe(1)Zn(1.2)O(x) (400)) exhibited higher catalytic activity and stability than the other catalysts for a 50 h reaction. Compared to the other catalysts, Na(0.2)/Fe(1)Zn(1.2)O(x) (400) enabled a higher number of active Fe carbides (Fe(5)C(2)) to intimately interact with the Na species, even though the catalyst had a lower total surface basicity based on surface area. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) showed a maximum hydrocarbon yield of 49.7% with a maximum olefin selectivity of 61.3% in the C1–C32 range. Examination of the reaction product mixture revealed that the Na(0.2)/Fe(1)Zn(1.2)O(x) catalysts converted α-olefins to branched paraffins (13.9–19.5%) via a series of isomerization, skeletal isomerization, and hydrogenation reactions. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) catalyst had a relatively low consumption rate of internal olefins compared to other catalysts, resulting in the lowest selectivity for branched paraffins. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) showed a maximum α-olefin yield (26.6%) in the range C2–C32, which was 27.9–50.0% higher than that of other catalysts. The α-olefin selectivity in the C5–C12 range for the Na(0.2)/Fe(1)Zn(1.2)O(x) (400) was 37.5% relative to the total α-olefins.
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spelling pubmed-90640402022-05-04 Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis Yang, Sunkyu Lee, Sungwoo Kang, Seok Chang Han, Seung Ju Jun, Ki-Won Lee, Kwan-Young Kim, Yong Tae RSC Adv Chemistry The production of linear alpha-olefins (α-olefins) is a practical way to increase the economic potential of the Fischer–Tropsch synthesis (FTS) because of their importance as chemical intermediates. Our study aimed to optimize Na-promoted Fe(1)Zn(1.2)O(x) catalysts such that they selectively converted syngas to linear α-olefins via FTS at 340 °C and 2.0 MPa. The Fe(1)Zn(1.2)O(x) catalysts were calcined at different temperatures from 350 to 700 °C before Na anchoring. The increase in the size of the ZnFe(2)O(4) crystals comprising the catalyst had a negative effect on the reducibility of Fe oxides and the particle size of Fe(5)C(2) during the reaction. The Na species in the catalyst restrained the reduction of Fe(1)Zn(1.2)O(x) but facilitated the formation of Fe(5)C(2). When pure Fe(1)Zn(1.2)O(x) was calcined at 400 °C, the corresponding catalyst (i.e., Na(0.2)/Fe(1)Zn(1.2)O(x) (400)) exhibited higher catalytic activity and stability than the other catalysts for a 50 h reaction. Compared to the other catalysts, Na(0.2)/Fe(1)Zn(1.2)O(x) (400) enabled a higher number of active Fe carbides (Fe(5)C(2)) to intimately interact with the Na species, even though the catalyst had a lower total surface basicity based on surface area. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) showed a maximum hydrocarbon yield of 49.7% with a maximum olefin selectivity of 61.3% in the C1–C32 range. Examination of the reaction product mixture revealed that the Na(0.2)/Fe(1)Zn(1.2)O(x) catalysts converted α-olefins to branched paraffins (13.9–19.5%) via a series of isomerization, skeletal isomerization, and hydrogenation reactions. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) catalyst had a relatively low consumption rate of internal olefins compared to other catalysts, resulting in the lowest selectivity for branched paraffins. The Na(0.2)/Fe(1)Zn(1.2)O(x) (400) showed a maximum α-olefin yield (26.6%) in the range C2–C32, which was 27.9–50.0% higher than that of other catalysts. The α-olefin selectivity in the C5–C12 range for the Na(0.2)/Fe(1)Zn(1.2)O(x) (400) was 37.5% relative to the total α-olefins. The Royal Society of Chemistry 2019-05-07 /pmc/articles/PMC9064040/ /pubmed/35519344 http://dx.doi.org/10.1039/c9ra02471a Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
Yang, Sunkyu
Lee, Sungwoo
Kang, Seok Chang
Han, Seung Ju
Jun, Ki-Won
Lee, Kwan-Young
Kim, Yong Tae
Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title_full Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title_fullStr Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title_full_unstemmed Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title_short Linear α-olefin production with Na-promoted Fe–Zn catalysts via Fischer–Tropsch synthesis
title_sort linear α-olefin production with na-promoted fe–zn catalysts via fischer–tropsch synthesis
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9064040/
https://www.ncbi.nlm.nih.gov/pubmed/35519344
http://dx.doi.org/10.1039/c9ra02471a
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