Pd-Cu/SiO2 catalyzed efficient hydrogen transfer of cyclohexanol and furfural platforms into cyclohexanone and furfuryl alcohol

被引:7
作者
Lan, Xufeng [1 ,2 ]
Wang, Suyao [1 ,2 ]
Zhang, Haotian [1 ,2 ]
Zhang, Yao [1 ,2 ]
Zhang, Yinmin [1 ,2 ]
Zhang, Yongfeng [1 ,2 ]
Wang, Jianjian [3 ,4 ]
Ding, Daqian [1 ,2 ]
机构
[1] Inner Mongolia Univ Technol, Chem Engn Coll, Key Lab Efficient Convers & Circular Econ Coal, Hohhot 010051, Inner Mongolia, Peoples R China
[2] Inner Mongolia Univ Technol, Chem Engn Coll, Key Lab Higher Educ Inst Resource Recycling, Hohhot 010051, Inner Mongolia, Peoples R China
[3] Chongqing Univ, Sch Chem & Chem Engn, Chongqing 400044, Peoples R China
[4] Chongqing Univ, Multiscale Porous Mat Ctr, Inst Adv Interdisciplinary Studies, Chongqing 401331, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrogen Transfer; Furfural; Cyclohexanol; Palladium; Copper; COPPER-CONTAINING CATALYSTS; TRANSFER DEHYDROGENATION; PHASE HYDROGENATION; OXIDATION-STATE; CU; BIOMASS; SBA-15; OXIDE; 2,5-DIMETHYLFURAN; PHENOL;
D O I
10.1016/j.fuel.2024.131278
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
High-performance and cost-effective designing of bimetallic catalysts is crucial for the efficient biomass-derived cyclic platforms conversion into fuel additives. To improve the hydrogen transfer efficiency between cyclohexanol and furfural, a Pd-Cu/SiO2 composite with self-synthesized mesoporous SiO2 support was developed and characterized. The state of Pd-Cu metal and catalyst surface were investigated through XRD, TEM, XPS, IR, H-2-TPR and NH3-TPD. The transfer hydrogenation of furfural into furfuryl alcohol through cyclohexanol dehydrogenation in the liquid phase was investigated and completed in hydrogen acceptor to donor molar ratios of 1:6-1:1.5, with significantly improved furfural hydrogenation capacity, achieving 84.6 % of furfuryl alcohol species molar yield with 97.7 % selectivity at 195 degrees C, 10 h, in 1:3 M ratio. The reaction was promoted in a molar ratio of 1:1 unprecedentedly without hydrogen wasted, and the reactant and product platforms were further investigated for the condensation synthesis of C-11 fuel additives. Reaction mechanism was investigated using 1,4-cyclohexanediol as model reactant at 240 and 280 degrees C, confirming the high selectivity of products originated from the non-planar adsorption state of reactant on the metal catalyst. This simple and active Pd-Cu bimetallic catalytic system may offer a cutting-edge liquid biofuel production pathway with potential industrial application due to its excellent stability and reproducibility.
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页数:14
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