Ag- and Cu-Promoted Mesoporous Ta-SiO2 Catalysts Prepared by Non-Hydrolytic Sol-Gel for the Conversion of Ethanol to Butadiene

被引:15
作者
Dochain, Denis D. [1 ]
Styskalik, Ales [1 ,2 ,3 ]
Debecker, Damien P. [1 ]
机构
[1] Univ Catholique Louvain UCLouvain, Inst Condensed Matter & Nanosci, Pl Louis Pasteur 1, B-1348 Louvain La Neuve, Belgium
[2] Masaryk Univ, Dept Chem, Kotlarska 2, CZ-61137 Brno, Czech Republic
[3] Masaryk Univ, CEITEC MU, Kamenice 5, CZ-62500 Brno, Czech Republic
基金
欧盟地平线“2020”;
关键词
Mesoporous metallosilicate; tantalum oxide; bioethanol; bifunctional catalysts; dehydration; dehydrogenation; MIXED-OXIDE CATALYSTS; HETEROGENEOUS CATALYSTS; 1,3-BUTADIENE; EPOXIDATION; BIOMASS; ELIMINATION; METATHESIS; OXIDATION; ROUTES; XPS;
D O I
10.3390/catal9110920
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The direct catalytic conversion of bioethanol to butadiene, also known as the Lebedev process, is one of the most promising solution to replace the petro-based production of this important bulk chemical. Considering the intricate reaction mechanism-where a combination of acid-catalyzed dehydration reactions and metal-catalyzed dehydrogenation have to take place simultaneously-tailor-made bifunctional catalysts are required. We propose to use non-hydrolytic sol-gel (NHSG) chemistry to prepare mesoporous Ta-SiO2 materials which are further promoted by Ag via impregnation. An acetamide elimination route is presented, starting from silicon tetraacetate and pentakis(dimethylamido)tantalum(V), in the presence of a Pluronic surfactant. The catalysts display advantageous texture, with specific surface area in the 600-1000 m(2) g(-1) range, large pore volume (0.6-1.0 mL g(-1)), an average pore diameter of 4 nm and only a small contribution from micropores. Using an array of characterization techniques, we show that NHSG allows achieving a high degree of dispersion of tantalum, mainly incorporated as single sites in the silica matrix. The presence of these monomeric TaOx active sites is responsible for the much higher dehydration ability, as compared to the corresponding catalyst prepared by impregnation of Ta onto a pristine silica support. We attempt to optimize the butadiene yield by changing the relative proportion of Ta and Ag and by tuning the space velocity. We also demonstrate that Ag or Cu can be introduced directly in one step, during the NHSG process. Copper doping is shown to be much more efficient than silver doping to guide the reaction towards the production of butadiene.
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页数:14
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