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Exploiting oxidative coupling of methane performed over La(CeMg)O catalysts with disordered defective cubic fluorite structure
The oxidative coupling of methane reaction to produce C 2 compounds was studied using La 2 (Ce 1− x Mg x ) 2 O 7− δ catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤ x ≤ 1.0), CH 4 /O 2 ratio, temperature, and WHSV. The partial substitution of Ce by Mg in t...
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Published in: | Catalysis science & technology 2021-07, Vol.11 (13), p.4471-4481 |
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creator | Petrolini, Davi D Marcos, Francielle F. C Lucrédio, Alessandra F Mastelaro, Valmor R Assaf, José M Assaf, Elisabete M |
description | The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV. The partial substitution of Ce by Mg in the structure modified the morphology, adjusted the reducibility, stabilized the Ce
3+
species, and provided different concentrations of basic sites, which allowed a 42% increase in the yield of C
2
, with ethylene as the major product. The catalyst with 0.4 Mg content in the structure provided C
2
selectivity of 52%, with CH
4
conversion of 28%, even under conditions richer in O
2
. The highest selectivity to C
2
(75%), with the highest selectivity to ethylene (39.1%), was achieved using a CH
4
: O
2
ratio of 8 : 1. In addition, it was possible to operate at milder temperatures (650 °C), with satisfactory CH
4
conversion (22%) and C
2
selectivity (54%). By decreasing the space velocity, the CH
4
conversion and C
2
selectivity decreased with an ethylene/ethane ratio of 3. The inhibitory effects of H
2
O and CO
2
were observed at lower space velocity.
The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV. |
doi_str_mv | 10.1039/d1cy00187f |
format | article |
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2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV. The partial substitution of Ce by Mg in the structure modified the morphology, adjusted the reducibility, stabilized the Ce
3+
species, and provided different concentrations of basic sites, which allowed a 42% increase in the yield of C
2
, with ethylene as the major product. The catalyst with 0.4 Mg content in the structure provided C
2
selectivity of 52%, with CH
4
conversion of 28%, even under conditions richer in O
2
. The highest selectivity to C
2
(75%), with the highest selectivity to ethylene (39.1%), was achieved using a CH
4
: O
2
ratio of 8 : 1. In addition, it was possible to operate at milder temperatures (650 °C), with satisfactory CH
4
conversion (22%) and C
2
selectivity (54%). By decreasing the space velocity, the CH
4
conversion and C
2
selectivity decreased with an ethylene/ethane ratio of 3. The inhibitory effects of H
2
O and CO
2
were observed at lower space velocity.
The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV.</description><identifier>ISSN: 2044-4753</identifier><identifier>EISSN: 2044-4761</identifier><identifier>DOI: 10.1039/d1cy00187f</identifier><ispartof>Catalysis science & technology, 2021-07, Vol.11 (13), p.4471-4481</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Petrolini, Davi D</creatorcontrib><creatorcontrib>Marcos, Francielle F. C</creatorcontrib><creatorcontrib>Lucrédio, Alessandra F</creatorcontrib><creatorcontrib>Mastelaro, Valmor R</creatorcontrib><creatorcontrib>Assaf, José M</creatorcontrib><creatorcontrib>Assaf, Elisabete M</creatorcontrib><title>Exploiting oxidative coupling of methane performed over La(CeMg)O catalysts with disordered defective cubic fluorite structure</title><title>Catalysis science & technology</title><description>The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV. The partial substitution of Ce by Mg in the structure modified the morphology, adjusted the reducibility, stabilized the Ce
3+
species, and provided different concentrations of basic sites, which allowed a 42% increase in the yield of C
2
, with ethylene as the major product. The catalyst with 0.4 Mg content in the structure provided C
2
selectivity of 52%, with CH
4
conversion of 28%, even under conditions richer in O
2
. The highest selectivity to C
2
(75%), with the highest selectivity to ethylene (39.1%), was achieved using a CH
4
: O
2
ratio of 8 : 1. In addition, it was possible to operate at milder temperatures (650 °C), with satisfactory CH
4
conversion (22%) and C
2
selectivity (54%). By decreasing the space velocity, the CH
4
conversion and C
2
selectivity decreased with an ethylene/ethane ratio of 3. The inhibitory effects of H
2
O and CO
2
were observed at lower space velocity.
The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV.</description><issn>2044-4753</issn><issn>2044-4761</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><sourceid/><recordid>eNqFT7FOAkEU3BhJJEpjb_JKLcBd7hSoCcYCYmNPlt238Mwee3n7FrnGb5eo0dJpZjIzmWSUujZ6ZHQ1u_fGdVqb6SScqf5Y1_Wwnjya81_9UF2oQc5v-oR6ZvR03Fcfi2MbEwntt5CO5K3QAcGl0sYvK0CDsrN7hBY5JG7QQzogw9LeznG1vXsBZ8XGLkuGd5IdeMqJPfKp6DGg-x4sG3IQYklMgpCFi5PCeKV6wcaMgx--VDdPi9f585CzW7dMjeVu_fer-i__BHmyU50</recordid><startdate>20210705</startdate><enddate>20210705</enddate><creator>Petrolini, Davi D</creator><creator>Marcos, Francielle F. C</creator><creator>Lucrédio, Alessandra F</creator><creator>Mastelaro, Valmor R</creator><creator>Assaf, José M</creator><creator>Assaf, Elisabete M</creator><scope/></search><sort><creationdate>20210705</creationdate><title>Exploiting oxidative coupling of methane performed over La(CeMg)O catalysts with disordered defective cubic fluorite structure</title><author>Petrolini, Davi D ; Marcos, Francielle F. C ; Lucrédio, Alessandra F ; Mastelaro, Valmor R ; Assaf, José M ; Assaf, Elisabete M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-rsc_primary_d1cy00187f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><creationdate>2021</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Petrolini, Davi D</creatorcontrib><creatorcontrib>Marcos, Francielle F. C</creatorcontrib><creatorcontrib>Lucrédio, Alessandra F</creatorcontrib><creatorcontrib>Mastelaro, Valmor R</creatorcontrib><creatorcontrib>Assaf, José M</creatorcontrib><creatorcontrib>Assaf, Elisabete M</creatorcontrib><jtitle>Catalysis science & technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Petrolini, Davi D</au><au>Marcos, Francielle F. C</au><au>Lucrédio, Alessandra F</au><au>Mastelaro, Valmor R</au><au>Assaf, José M</au><au>Assaf, Elisabete M</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Exploiting oxidative coupling of methane performed over La(CeMg)O catalysts with disordered defective cubic fluorite structure</atitle><jtitle>Catalysis science & technology</jtitle><date>2021-07-05</date><risdate>2021</risdate><volume>11</volume><issue>13</issue><spage>4471</spage><epage>4481</epage><pages>4471-4481</pages><issn>2044-4753</issn><eissn>2044-4761</eissn><abstract>The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV. The partial substitution of Ce by Mg in the structure modified the morphology, adjusted the reducibility, stabilized the Ce
3+
species, and provided different concentrations of basic sites, which allowed a 42% increase in the yield of C
2
, with ethylene as the major product. The catalyst with 0.4 Mg content in the structure provided C
2
selectivity of 52%, with CH
4
conversion of 28%, even under conditions richer in O
2
. The highest selectivity to C
2
(75%), with the highest selectivity to ethylene (39.1%), was achieved using a CH
4
: O
2
ratio of 8 : 1. In addition, it was possible to operate at milder temperatures (650 °C), with satisfactory CH
4
conversion (22%) and C
2
selectivity (54%). By decreasing the space velocity, the CH
4
conversion and C
2
selectivity decreased with an ethylene/ethane ratio of 3. The inhibitory effects of H
2
O and CO
2
were observed at lower space velocity.
The oxidative coupling of methane reaction to produce C
2
compounds was studied using La
2
(Ce
1−
x
Mg
x
)
2
O
7−
δ
catalysts with disordered defective cubic fluorite structures, varying the Mg content (0.0 ≤
x
≤ 1.0), CH
4
/O
2
ratio, temperature, and WHSV.</abstract><doi>10.1039/d1cy00187f</doi><tpages>11</tpages></addata></record> |
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source | Royal Society of Chemistry:Jisc Collections:Royal Society of Chemistry Read and Publish 2022-2024 (reading list) |
title | Exploiting oxidative coupling of methane performed over La(CeMg)O catalysts with disordered defective cubic fluorite structure |
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