Catalytic Valorisation of Biomass-Derived Levulinic Acid to Biofuel Additive γ-Valerolactone: Influence of Copper Loading on Silica Support

被引:11
作者
Boddula, Rajender [1 ]
Shanmugam, Paramasivam [2 ]
Srivatsava, Rajesh K. [3 ]
Tabassum, Nabila [4 ]
Pothu, Ramyakrishna [5 ]
Naik, Ramachandra [6 ]
Saran, Aditya [7 ]
Viswanadham, Balaga [8 ]
Radwan, Ahmed Bahgat [1 ]
Al-Qahtani, Noora [1 ]
机构
[1] Qatar Univ, Ctr Adv Mat CAM, Doha 2713, Qatar
[2] Thammasat Univ, Fac Sci & Technol, Dept Chem, Pathum Thani 12120, Thailand
[3] GITAM, Dept Biotechnol, GST, Visakhapatnam 530045, India
[4] Shiv Nadar Univ, Dept Chem Engn, Greater Noida 201314, India
[5] Hunan Univ, Coll Chem & Chem Engn, Sch Phys & Elect, Changsha 410082, Peoples R China
[6] New Horizon Coll Engn, Dept Phys, Bangalore 560103, India
[7] Marwadi Univ, Dept Microbiol, Rajkot 360003, India
[8] GMR Inst Technol, Dept Basic Sci & Humanities, Rajam 532127, India
来源
REACTIONS | 2023年 / 4卷 / 03期
关键词
biomass; gamma-valerolactone; biofuel additive; green solvent; vapour-phase hydrogenation; selectivity; VAPOR-PHASE HYDROGENATION; NONNOBLE METAL-CATALYSTS; FORMIC-ACID; SELECTIVE HYDROGENATION; CARBOHYDRATE BIOMASS; CONVERSION; RU; HYDROXYAPATITE; TRANSFORMATION; HYDROTALCITE;
D O I
10.3390/reactions4030028
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
gamma-valerolactone (GVL) is a crucial chemical feedstock used in the production of fuel additives, renewable fuels, and fine chemicals alternative to petroleum-based solvents and chemicals, supporting the transition to sustainable energy solutions. It is promptly acquired by hydrogenating levulinic acid (LA) in a gaseous or liquid phase with a homogeneous or heterogeneous catalyst using a variety of recognized catalytic processes. Herein, this work focuses on the use of silica-supported copper (Cu/SiO2) catalysts for the gas-phase hydrogenation of LA to GVL under mild reaction conditions. The study analyzes how copper loading can affect the catalytic activity of the Cu/SiO2, while the flow rate of LA, time-on-stream, reaction temperature, and LA concentration affect the catalytic efficiency. The SiO2 support's various Cu loadings are crucial for adjusting the catalytic hydrogenation activity. One of the studied catalysts, a 5 wt% Cu/SiO2 catalyst, demonstrated similar to 81% GVL selectivity with similar to 78% LA conversion and demonstrated stability for similar to 8 h while operating at atmospheric pressure and temperature (265 degrees C) and 0.5 mL/h of LA flow rate. The ability to activate hydrogen, high amount of acidic sites, and surface area were all discovered to be advantageous for increased GVL selectivity.
引用
收藏
页码:465 / 477
页数:13
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