TY - JOUR
T1 - Bimetallic Ni–Cu/CeO2–Al2O3 catalysts for conversion of ethanol to higher alcohols
AU - Rathinasamy, Vinayagamoorthi
AU - Arjunan, Ariharan
AU - Ramaswamy, Krishnamurthy Konda
AU - Balasubramanian, Viswanathan
AU - Kannan, Shanthi
N1 - Publisher Copyright:
© 2023, Akadémiai Kiadó, Budapest, Hungary.
PY - 2023/4
Y1 - 2023/4
N2 - A sustainable route for the synthesis of butanol and higher alcohols via condensation of bio-ethanol has been investigated on a series of modified nickel on alumina catalysts. To maximize the selectivity for butanol, alumina support has been modified with ceria (5 wt% of alumina) to enhance basicity. Copper is added as the second metal, to promote dehydrogenation-hydrogenation functionality. Ni–Cu bi-metallic catalysts with varying proportions of the metals, i.e., bimetallic 5.5% Cu-2.5% Ni, 4% Cu-4% Ni and 2% Cu-6% Ni catalysts and 8% Cu, 8% Ni (all wt%) mono metallic catalysts, supported on ceria modified Al2O3, have been prepared by wet impregnation and characterized by XRD, BET, TEM, NH3– and CO2 TPD, H2–TPR and XPS. Condensation of ethanol has been carried out in Parr reactor, in batch mode (8 h, at 200 °C, after pressurization with nitrogen (10 bar). Mono metallic Ni displays ethanol conversion of 41%, with butanol selectivity of 48.6%. Whereas, mono metallic Cu catalyst, under identical reaction conditions, displays high butanol selectivity (64%) but very low ethanol conversion (18%). Bimetallic catalyst with composition 5.5% Cu-2.5% Ni, displays higher butanol selectivity of 55.6% with conversion at 32.2%. Thus, by optimization of Cu and Ni composition and support acidity/basicity, it is possible to maximize butanol selectivity. XPS and TPR studies indicate Ni–Cu alloy formation, especially in the compositions, 4% Ni-4% Cu, and 2.5% Ni-5.5% Cu. Presence Ni–Cu alloys, moderation of acidity and increase in medium and strong basic sites facilitate higher butanol selectivity. Graphical Abstract: [Figure not available: see fulltext.]
AB - A sustainable route for the synthesis of butanol and higher alcohols via condensation of bio-ethanol has been investigated on a series of modified nickel on alumina catalysts. To maximize the selectivity for butanol, alumina support has been modified with ceria (5 wt% of alumina) to enhance basicity. Copper is added as the second metal, to promote dehydrogenation-hydrogenation functionality. Ni–Cu bi-metallic catalysts with varying proportions of the metals, i.e., bimetallic 5.5% Cu-2.5% Ni, 4% Cu-4% Ni and 2% Cu-6% Ni catalysts and 8% Cu, 8% Ni (all wt%) mono metallic catalysts, supported on ceria modified Al2O3, have been prepared by wet impregnation and characterized by XRD, BET, TEM, NH3– and CO2 TPD, H2–TPR and XPS. Condensation of ethanol has been carried out in Parr reactor, in batch mode (8 h, at 200 °C, after pressurization with nitrogen (10 bar). Mono metallic Ni displays ethanol conversion of 41%, with butanol selectivity of 48.6%. Whereas, mono metallic Cu catalyst, under identical reaction conditions, displays high butanol selectivity (64%) but very low ethanol conversion (18%). Bimetallic catalyst with composition 5.5% Cu-2.5% Ni, displays higher butanol selectivity of 55.6% with conversion at 32.2%. Thus, by optimization of Cu and Ni composition and support acidity/basicity, it is possible to maximize butanol selectivity. XPS and TPR studies indicate Ni–Cu alloy formation, especially in the compositions, 4% Ni-4% Cu, and 2.5% Ni-5.5% Cu. Presence Ni–Cu alloys, moderation of acidity and increase in medium and strong basic sites facilitate higher butanol selectivity. Graphical Abstract: [Figure not available: see fulltext.]
KW - Ceria-alumina support
KW - Cu-Ni alloy
KW - Cu-Ni bimetallic catalyst
KW - Ethanol to butanol
KW - Guerbet reaction
UR - https://www.scopus.com/pages/publications/85148618534
U2 - 10.1007/s11144-023-02347-6
DO - 10.1007/s11144-023-02347-6
M3 - Article
AN - SCOPUS:85148618534
SN - 1878-5190
VL - 136
SP - 713
EP - 725
JO - Reaction Kinetics, Mechanisms and Catalysis
JF - Reaction Kinetics, Mechanisms and Catalysis
IS - 2
ER -