Production of γ-valerolactone over mesoporous CuO catalysts using formic acid as the hydrogen source

被引:3
作者
Ayashi, Neda [1 ]
Chermahini, Alireza Najafi [1 ]
Ramsheh, Nasim Amiri [1 ]
Luque, Rafael [2 ,3 ]
机构
[1] Isfahan Univ Technol, Dept Chem, Esfahan 8415483111, Iran
[2] Univ Cordoba, Dept Quim Organ, Campus Rabanales,Edificio Marie Curie C-3, E-14014 Cordoba, Spain
[3] Peoples Friendship Univ Russia, RUDN Univ, 6 Miklukho Maklaya Str, Moscow 117198, Russia
基金
美国国家科学基金会;
关键词
LEVULINIC ACID; ONE-POT; COPPER-OXIDE; BIOMASS; CONVERSION; DERIVATIVES; PLATFORM; LIQUID; ENERGY; FUELS;
D O I
10.1039/d2re00192f
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In the present study, the conversion of levulinic acid (LA), butyl levulinate (BL), and ethyl levulinate (EL) to valuable biomass-derived compound gamma-valerolactone (GVL) is studied. A series of mesoporous CuO catalysts prepared through the hard template method were used in combination with formic acid (FA) as the hydrogen donor for the reduction of LA and levulinate esters. The catalysts are characterized using analytical and physical methods such as XRD, FESEM-EDX, and nitrogen adsorption-desorption, hydrogen temperature-programmed reduction, and TEM techniques. Among the samples, mesoporous CuO which was reduced under a hydrogen atmosphere exhibited higher activity in the cascade formic acid decomposition and hydrogen transfer to alkyl levulinates, followed by the ring closure and formation of gamma-valerolactone. The effect of influential factors including the amount of catalyst, reaction temperature, levulinic acid and alkyl levulinate amount to formic acid ratio, and reaction time on the conversion of substrates and GVL yield was also investigated. According to the obtained results, 50 mg of the mesoporous CuO catalyst, 180 degrees C as the reaction temperature, and 5 h as the reaction time were selected as the optimum reaction conditions.
引用
收藏
页码:2385 / 2398
页数:14
相关论文
共 62 条
[1]   Process design and techno-economic evaluation for the production of platform chemical for hydrocarbon fuels from lignocellulosic biomass using biomass-derived γ-valerolactone [J].
Ahmad, Nauman ;
Ahmad, Nabeel ;
Ahmed, Usama .
RENEWABLE ENERGY, 2020, 161 :750-755
[2]  
Amarasekara A.S., 2018, BIOFUELS-UK, P1
[3]   Efficient Solvent-Free Hydrogenation of Levulinic Acid to γ-Valerolactone by Pyrazolylphosphite and Pyrazolylphosphinite Ruthenium(II) Complexes [J].
Amenuvor, Gershon ;
Makhubela, Banothile C. E. ;
Darkwa, James .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2016, 4 (11) :6010-6018
[4]   Biomass as renewable feedstock in standard refinery units. Feasibility, opportunities and challenges [J].
Antonio Melero, Juan ;
Iglesias, Jose ;
Garcia, Alicia .
ENERGY & ENVIRONMENTAL SCIENCE, 2012, 5 (06) :7393-7420
[5]  
Ashokraju M, 2018, J CHEM SCI, V130, DOI 10.1007/s12039-018-1418-3
[6]   Biomass conversion to alkyl levulinates using heteropoly acid carbon mesoporous composites [J].
Ayashi, Neda ;
Chermahini, Alireza Najafi ;
Saraji, Mohammad .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2022, 160 :988-1000
[7]   Alumina-coated mesoporous silica SBA-15 as a solid catalyst for catalytic conversion of fructose into liquid biofuel candidate ethyl levulinate [J].
Babaei, Zahra ;
Chermahini, Alireza Najafi ;
Dinari, Mohammad .
CHEMICAL ENGINEERING JOURNAL, 2018, 352 :45-52
[8]   Preparation of mesoporous Cu/ZnO catalyst and its application in low-temperature methanol synthesis [J].
Bao, Jun ;
Liu, Zhenlin ;
Zhang, Yi ;
Tsubaki, Noritatsu .
CATALYSIS COMMUNICATIONS, 2008, 9 (05) :913-918
[9]   Highly selective etherification of fructose and 5-hydroxymethylfurfural over a novel Pd-Ru/MXene catalyst for sustainable liquid fuel production [J].
Bharath, Govindan ;
Rambabu, Krishnamoorthy ;
Hai, Abdul ;
Morajkar, Pranay P. ;
Salkar, Akshay, V ;
Hasan, Shadi W. ;
Show, Pau Loke ;
Banat, Fawzi .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2021, 45 (10) :14680-14691
[10]   Towards Sustainable Production of Formic Acid [J].
Bulushev, Dmitri A. ;
Ross, Julian R. H. .
CHEMSUSCHEM, 2018, 11 (05) :821-836