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Catalytic upgrading of biomass-derived vapors on carbon aerogel-supported Ni: Effect of temperature, metal cluster size and catalyst-to-biomass ratio

A comprehensive study of carbon aerogel-supported nickel (Ni/CAG) in the catalytic fast pyrolysis (CFP) of torrefied Eucalyptus globulus was performed in a micropyrolysis unit (Py-GCMS). Effects of pyrolysis temperatures (450–600 °C), catalyst-to-biomass ratio (1:1 

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Published in:Fuel processing technology 2018-09, Vol.178, p.251-261
Main Authors: Arteaga-Pérez, Luis E., Jiménez, Romel, Grob, Nicolas, Gómez, Oscar, Romero, Romina, Ronsse, Frederik
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cited_by cdi_FETCH-LOGICAL-c371t-c1ffe824cdc3b2d26faefec9dbede2ac6c1f1fe336c674129270bbaf38ae09693
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container_title Fuel processing technology
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creator Arteaga-Pérez, Luis E.
Jiménez, Romel
Grob, Nicolas
Gómez, Oscar
Romero, Romina
Ronsse, Frederik
description A comprehensive study of carbon aerogel-supported nickel (Ni/CAG) in the catalytic fast pyrolysis (CFP) of torrefied Eucalyptus globulus was performed in a micropyrolysis unit (Py-GCMS). Effects of pyrolysis temperatures (450–600 °C), catalyst-to-biomass ratio (1:1 
doi_str_mv 10.1016/j.fuproc.2018.05.036
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Effects of pyrolysis temperatures (450–600 °C), catalyst-to-biomass ratio (1:1 &lt; C-to-B &lt; 10:1) and metal cluster sizes (9.6 &lt; Dpi &lt; 21) on upgrading reactions were analyzed. Catalysts were characterized by N2 adsorption-desorption at 77 K, X-ray diffraction (XRD) and Transmission Electron Microscopy (TEM). Regardless the use of catalysts, the pyrolysis vapors produced from torrefied biomass were depleted in carboxylic acids (selectivity &lt; 7%). Furthermore, the CFP decreased the selectivity to furans and ketones by almost 50%, while phenols increased in a similar proportion. Despite the similarities in the selectivity distribution of these functional groups in all the CFP experiments, their internal composition was rather different owing to the changes in temperature, C-to-B ratio and catalyst cluster sizes. Ni/CAG was active for hydrogenation under H2-depleted atmosphere, presumably by a synergistic effect between water gas shift and reforming reactions with transalkylation and decarbonylation of phenolics and furanics. It was demonstrated that metal cluster sizes influenced the reaction routes by favoring hydrogenation on metal facets and deoxygenation on step/corners sites. •Improved bio-oil composition by torrefaction pretreatment of Eucalyptus globulus.•Upgrading reactions increased above 550 °C, for Ni/CAG-catalyzed pyrolysis.•Ni/CAG was active for hydrogenation under H2-depleted atmosphere.•Ni/CAG promoted hydrogenation on metal facets and deoxygenation on step/corners.</description><identifier>ISSN: 0378-3820</identifier><identifier>EISSN: 1873-7188</identifier><identifier>DOI: 10.1016/j.fuproc.2018.05.036</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Adsorption ; Aerogels ; Biomass ; Carbon ; Carbon aerogel ; Carboxylic acids ; Catalysis ; Catalysts ; Catalytic fast pyrolysis ; Deoxygenation ; Eucalyptus ; Functional groups ; Furans ; Hydrogenation ; Ketones ; Metal clusters ; Nickel ; Phenols ; Pyrolysis ; Reaction route ; Reforming ; Selectivity ; Studies ; Synergistic effect ; Temperature effects ; Torrefaction ; Transalkylation ; Transmission electron microscopy ; Water gas ; X-ray diffraction</subject><ispartof>Fuel processing technology, 2018-09, Vol.178, p.251-261</ispartof><rights>2018 Elsevier B.V.</rights><rights>Copyright Elsevier Science Ltd. 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Effects of pyrolysis temperatures (450–600 °C), catalyst-to-biomass ratio (1:1 &lt; C-to-B &lt; 10:1) and metal cluster sizes (9.6 &lt; Dpi &lt; 21) on upgrading reactions were analyzed. Catalysts were characterized by N2 adsorption-desorption at 77 K, X-ray diffraction (XRD) and Transmission Electron Microscopy (TEM). Regardless the use of catalysts, the pyrolysis vapors produced from torrefied biomass were depleted in carboxylic acids (selectivity &lt; 7%). Furthermore, the CFP decreased the selectivity to furans and ketones by almost 50%, while phenols increased in a similar proportion. Despite the similarities in the selectivity distribution of these functional groups in all the CFP experiments, their internal composition was rather different owing to the changes in temperature, C-to-B ratio and catalyst cluster sizes. Ni/CAG was active for hydrogenation under H2-depleted atmosphere, presumably by a synergistic effect between water gas shift and reforming reactions with transalkylation and decarbonylation of phenolics and furanics. It was demonstrated that metal cluster sizes influenced the reaction routes by favoring hydrogenation on metal facets and deoxygenation on step/corners sites. •Improved bio-oil composition by torrefaction pretreatment of Eucalyptus globulus.•Upgrading reactions increased above 550 °C, for Ni/CAG-catalyzed pyrolysis.•Ni/CAG was active for hydrogenation under H2-depleted atmosphere.•Ni/CAG promoted hydrogenation on metal facets and deoxygenation on step/corners.</description><subject>Adsorption</subject><subject>Aerogels</subject><subject>Biomass</subject><subject>Carbon</subject><subject>Carbon aerogel</subject><subject>Carboxylic acids</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Catalytic fast pyrolysis</subject><subject>Deoxygenation</subject><subject>Eucalyptus</subject><subject>Functional groups</subject><subject>Furans</subject><subject>Hydrogenation</subject><subject>Ketones</subject><subject>Metal clusters</subject><subject>Nickel</subject><subject>Phenols</subject><subject>Pyrolysis</subject><subject>Reaction route</subject><subject>Reforming</subject><subject>Selectivity</subject><subject>Studies</subject><subject>Synergistic effect</subject><subject>Temperature effects</subject><subject>Torrefaction</subject><subject>Transalkylation</subject><subject>Transmission electron microscopy</subject><subject>Water gas</subject><subject>X-ray diffraction</subject><issn>0378-3820</issn><issn>1873-7188</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp9kc1KAzEUhYMoWKtv4CLg1oz5aTMzLgQp_oHoRtchk9yUlHYyJpmCvofva0q7dnUX95zzce9B6JLRilEmb1aVG4cYTMUpayo6r6iQR2jCmlqQmjXNMZpQUTdENJyeorOUVpTS-bytJ-h3obNef2dv8Dgso7a-X-LgcOfDRqdELES_BYu3eggx4dBjo2NXhoYYlrAmaRzKJhfJm7_FD86BybuADJsBos5jhGu8gQLBZj2mDBEn_wNY97ZE7dgpkxzIAYiLxYdzdOL0OsHFYU7R5-PDx-KZvL4_vSzuX4kRNcvEsIJr-MxYIzpuuXQaCr-1HVjg2sgiYA6EkEbWM8ZbXtOu0040GmgrWzFFV_vc8r2vEVJWqzDGviAVZ0xIygSVRTXbq0wMKUVwaoh-o-O3YlTtClArtS9A7QpQdK5KAcV2t7dBuWDrIapkPPQGrI_lScoG_3_AH_CGlak</recordid><startdate>20180901</startdate><enddate>20180901</enddate><creator>Arteaga-Pérez, Luis E.</creator><creator>Jiménez, Romel</creator><creator>Grob, Nicolas</creator><creator>Gómez, Oscar</creator><creator>Romero, Romina</creator><creator>Ronsse, Frederik</creator><general>Elsevier B.V</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>L7M</scope><orcidid>https://orcid.org/0000-0003-3982-4165</orcidid><orcidid>https://orcid.org/0000-0002-8238-3900</orcidid><orcidid>https://orcid.org/0000-0003-0963-1637</orcidid></search><sort><creationdate>20180901</creationdate><title>Catalytic upgrading of biomass-derived vapors on carbon aerogel-supported Ni: Effect of temperature, metal cluster size and catalyst-to-biomass ratio</title><author>Arteaga-Pérez, Luis E. ; 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Effects of pyrolysis temperatures (450–600 °C), catalyst-to-biomass ratio (1:1 &lt; C-to-B &lt; 10:1) and metal cluster sizes (9.6 &lt; Dpi &lt; 21) on upgrading reactions were analyzed. Catalysts were characterized by N2 adsorption-desorption at 77 K, X-ray diffraction (XRD) and Transmission Electron Microscopy (TEM). Regardless the use of catalysts, the pyrolysis vapors produced from torrefied biomass were depleted in carboxylic acids (selectivity &lt; 7%). Furthermore, the CFP decreased the selectivity to furans and ketones by almost 50%, while phenols increased in a similar proportion. Despite the similarities in the selectivity distribution of these functional groups in all the CFP experiments, their internal composition was rather different owing to the changes in temperature, C-to-B ratio and catalyst cluster sizes. Ni/CAG was active for hydrogenation under H2-depleted atmosphere, presumably by a synergistic effect between water gas shift and reforming reactions with transalkylation and decarbonylation of phenolics and furanics. It was demonstrated that metal cluster sizes influenced the reaction routes by favoring hydrogenation on metal facets and deoxygenation on step/corners sites. •Improved bio-oil composition by torrefaction pretreatment of Eucalyptus globulus.•Upgrading reactions increased above 550 °C, for Ni/CAG-catalyzed pyrolysis.•Ni/CAG was active for hydrogenation under H2-depleted atmosphere.•Ni/CAG promoted hydrogenation on metal facets and deoxygenation on step/corners.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.fuproc.2018.05.036</doi><tpages>11</tpages><orcidid>https://orcid.org/0000-0003-3982-4165</orcidid><orcidid>https://orcid.org/0000-0002-8238-3900</orcidid><orcidid>https://orcid.org/0000-0003-0963-1637</orcidid></addata></record>
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ispartof Fuel processing technology, 2018-09, Vol.178, p.251-261
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1873-7188
language eng
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subjects Adsorption
Aerogels
Biomass
Carbon
Carbon aerogel
Carboxylic acids
Catalysis
Catalysts
Catalytic fast pyrolysis
Deoxygenation
Eucalyptus
Functional groups
Furans
Hydrogenation
Ketones
Metal clusters
Nickel
Phenols
Pyrolysis
Reaction route
Reforming
Selectivity
Studies
Synergistic effect
Temperature effects
Torrefaction
Transalkylation
Transmission electron microscopy
Water gas
X-ray diffraction
title Catalytic upgrading of biomass-derived vapors on carbon aerogel-supported Ni: Effect of temperature, metal cluster size and catalyst-to-biomass ratio
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