Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation
Precursors materials with formula, La 1− x Ce x Al 0.18 Ni 0.82 O 3 ( x = 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content ( x = 0.0; 0.1), the perovskite struc...
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creator | Morales, Ruddy Campos, Cristian H Fierro, J. L. G Fraga, Marco A Pecchi, Gina |
description | Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content (
x
= 0.0; 0.1), the perovskite structure was obtained, whereas for a higher Ce content (
x
= 0.5; 0.7), an ordinary CeO
2
-La
2
O
3
solid dissolution with no perovskite structure were obtained. Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure (
x
= 0.0; 0.1) and the CeO
2
-La
2
O
3
solid dissolution allows a Ni reduction of ∼40% of Ni (
x
= 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure (
x
= 0.0; 0.1) and solid dissolution (
x
= 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor (
x
= 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium.
Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. |
doi_str_mv | 10.1039/c6ra13395a |
format | Article |
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1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content (
x
= 0.0; 0.1), the perovskite structure was obtained, whereas for a higher Ce content (
x
= 0.5; 0.7), an ordinary CeO
2
-La
2
O
3
solid dissolution with no perovskite structure were obtained. Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure (
x
= 0.0; 0.1) and the CeO
2
-La
2
O
3
solid dissolution allows a Ni reduction of ∼40% of Ni (
x
= 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure (
x
= 0.0; 0.1) and solid dissolution (
x
= 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor (
x
= 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium.
Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol.</description><identifier>ISSN: 2046-2069</identifier><identifier>EISSN: 2046-2069</identifier><identifier>DOI: 10.1039/c6ra13395a</identifier><language>eng</language><subject>Catalysts ; Dissolution ; Hydrogenation ; Leaching ; Nickel ; Perovskite structure ; Precursors ; Xylose</subject><ispartof>RSC advances, 2016-01, Vol.6 (72), p.67817-67826</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c352t-876646f797eda8e0b8cf8a7248c9af59b9b0e7f3fb07fba2a6ed81e178a220d43</citedby><cites>FETCH-LOGICAL-c352t-876646f797eda8e0b8cf8a7248c9af59b9b0e7f3fb07fba2a6ed81e178a220d43</cites><orcidid>0000-0001-8592-5384</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids></links><search><creatorcontrib>Morales, Ruddy</creatorcontrib><creatorcontrib>Campos, Cristian H</creatorcontrib><creatorcontrib>Fierro, J. L. G</creatorcontrib><creatorcontrib>Fraga, Marco A</creatorcontrib><creatorcontrib>Pecchi, Gina</creatorcontrib><title>Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation</title><title>RSC advances</title><description>Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content (
x
= 0.0; 0.1), the perovskite structure was obtained, whereas for a higher Ce content (
x
= 0.5; 0.7), an ordinary CeO
2
-La
2
O
3
solid dissolution with no perovskite structure were obtained. Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure (
x
= 0.0; 0.1) and the CeO
2
-La
2
O
3
solid dissolution allows a Ni reduction of ∼40% of Ni (
x
= 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure (
x
= 0.0; 0.1) and solid dissolution (
x
= 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor (
x
= 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium.
Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol.</description><subject>Catalysts</subject><subject>Dissolution</subject><subject>Hydrogenation</subject><subject>Leaching</subject><subject>Nickel</subject><subject>Perovskite structure</subject><subject>Precursors</subject><subject>Xylose</subject><issn>2046-2069</issn><issn>2046-2069</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNpNkNtLwzAUxoMoOHQvvgt9FKGaS5smj2N4g4Ei-lxO08TFZU1NMrH_vZ0T53k5tx8fHx9CZwRfEczkteIBCGOyhAM0objgOcVcHv6bj9E0xnc8Fi8J5WSC3JMO_jOubNIZxKyzaqVdpiCBG2LK-qDVJkQfsjyz6x5Uyny3f8cEjXU2Ddvr1-B8HFU-NtpvYt4vYdyWQxv8m-4gWd-doiMDLurpbz9Br7c3L_P7fPF49zCfLXLFSppyUXFecFPJSrcgNG6EMgIqWgglwZSykQ3WlWGmwZVpgALXrSCaVAIoxW3BTtDFTrcPfnQTU722UWnnoNtaq4lgJadUSj6ilztUBR9j0Kbug11DGGqC622q9Zw_z35SnY3w-Q4OUf1x-9TZN6ymdp4</recordid><startdate>20160101</startdate><enddate>20160101</enddate><creator>Morales, Ruddy</creator><creator>Campos, Cristian H</creator><creator>Fierro, J. L. G</creator><creator>Fraga, Marco A</creator><creator>Pecchi, Gina</creator><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><orcidid>https://orcid.org/0000-0001-8592-5384</orcidid></search><sort><creationdate>20160101</creationdate><title>Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation</title><author>Morales, Ruddy ; Campos, Cristian H ; Fierro, J. L. G ; Fraga, Marco A ; Pecchi, Gina</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c352t-876646f797eda8e0b8cf8a7248c9af59b9b0e7f3fb07fba2a6ed81e178a220d43</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Catalysts</topic><topic>Dissolution</topic><topic>Hydrogenation</topic><topic>Leaching</topic><topic>Nickel</topic><topic>Perovskite structure</topic><topic>Precursors</topic><topic>Xylose</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Morales, Ruddy</creatorcontrib><creatorcontrib>Campos, Cristian H</creatorcontrib><creatorcontrib>Fierro, J. L. G</creatorcontrib><creatorcontrib>Fraga, Marco A</creatorcontrib><creatorcontrib>Pecchi, Gina</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>RSC advances</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Morales, Ruddy</au><au>Campos, Cristian H</au><au>Fierro, J. L. G</au><au>Fraga, Marco A</au><au>Pecchi, Gina</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation</atitle><jtitle>RSC advances</jtitle><date>2016-01-01</date><risdate>2016</risdate><volume>6</volume><issue>72</issue><spage>67817</spage><epage>67826</epage><pages>67817-67826</pages><issn>2046-2069</issn><eissn>2046-2069</eissn><abstract>Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol. For the Ce free and lower Ce content (
x
= 0.0; 0.1), the perovskite structure was obtained, whereas for a higher Ce content (
x
= 0.5; 0.7), an ordinary CeO
2
-La
2
O
3
solid dissolution with no perovskite structure were obtained. Under the reduction conditions, the perovskite structure leads to ∼30% of metallic Ni without any loss of the perovskite structure (
x
= 0.0; 0.1) and the CeO
2
-La
2
O
3
solid dissolution allows a Ni reduction of ∼40% of Ni (
x
= 0.5; 0.7). As expected, the similar reduced Ni content does not show large differences in the aqueous-phase xylose hydrogenation product distribution, or large difference in the precursors. The perovskite structure (
x
= 0.0; 0.1) and solid dissolution (
x
= 0.5; 0.7) highlight the importance of the perovskite structure in the remarkable leaching resistance showed by the Ni perovskite-precursor (
x
= 0.0; 0.1) catalysts, showing no Ni leaching over 6 h of reaction in an aqueous medium.
Precursors materials with formula, La
1−
x
Ce
x
Al
0.18
Ni
0.82
O
3
(
x
= 0.0, 0.1, 0.5, 0.7), were successfully used as precursors to prepare Ni nanoclusters to be used as catalysts in the hydrogenation of xylose to xylitol.</abstract><doi>10.1039/c6ra13395a</doi><tpages>1</tpages><orcidid>https://orcid.org/0000-0001-8592-5384</orcidid></addata></record> |
fulltext | fulltext |
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language | eng |
recordid | cdi_rsc_primary_c6ra13395a |
source | Royal Society Of Chemistry Journals 2008- |
subjects | Catalysts Dissolution Hydrogenation Leaching Nickel Perovskite structure Precursors Xylose |
title | Perovskite as nickel catalyst precursor - impact on catalyst stability on xylose aqueous-phase hydrogenation |
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