Catalytic Hydrogenation, Hydrodeoxygenation, and Hydrocracking Processes of a Lignin Monomer Model Compound Eugenol over Magnetic Ru/C–Fe2O3 and Mechanistic Reaction Microkinetics
Autor: | Darko Makovec, Ana Bjelić, Miha Grilc, Blaž Likozar, Andraž Kocjan, Sašo Gyergyek |
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Jazyk: | angličtina |
Rok vydání: | 2018 |
Předmět: |
structure–activity relationship
recyclable ruthenium catalyst chemistry.chemical_element 02 engineering and technology 010402 general chemistry lcsh:Chemical technology 01 natural sciences Catalysis law.invention lcsh:Chemistry chemistry.chemical_compound Hydrogenolysis law Organic chemistry biomass-derived chemicals Calcination lcsh:TP1-1185 Physical and Theoretical Chemistry Deoxygenation hydroprocessing Chemistry 021001 nanoscience & nanotechnology Product distribution 0104 chemical sciences Ruthenium intrinsic kinetics modelling Monomer lcsh:QD1-999 heteroatom removal 0210 nano-technology Hydrodeoxygenation |
Zdroj: | Catalysts Volume 8 Issue 10 Catalysts, Vol 8, Iss 10, p 425 (2018) |
ISSN: | 2073-4344 |
DOI: | 10.3390/catal8100425 |
Popis: | Conversion of waste lignocellulosic (LC) biomass, a widely-available low-cost feedstock, into value-added biobased chemicals (and biofuels) has been gaining much attention recently. Therefore, the present lignin valorisation study was aimed at developing magnetically-separable highly-active catalysts for hydrodeoxygenation (HDO), also proposing surface chemical kinetics. Five carbonaceous substrate-deposited Ru were synthesised and tested for the HDO of monomer moiety eugenol. Their annealing temperatures differed, specifically between 300 and 750 ° C, while one was not subjected to calcination. Experiments revealed the substantial influence of annealing temperature on the product distribution. Namely, fresh nonannealed nanocomposites were not active for hydrogenolysis. By further pretreatment increase, hydrogenation and, exclusively, the deoxygenation of saturated cyclic species, were enhanced, these being more promoted considering rates and yields than commercial carbon-supported ruthenium. Over 80 mol% of 4-propyl-cylohexanol and propyl-cyclohexane could be formed over the samples, treated at 500 and 600 ° C, for 100 and 125 min, respectively, under 275 ° C and 5 MPa of reactor hydrogen pressure. Interestingly, a notable 4-propyl-phenol amount was produced upon 750 ° C pretreating. The intrinsic microkinetic model, developed previously, was applied to determine relevant turnover parameters. Calculated modelling results indicated a 47- and 10-fold greater demethoxylation and dehydroxylation mechanism ability upon the reheatingpreheating at 600 ° C in comparison to industrial (heterogeneous) Ru/C. |
Databáze: | OpenAIRE |
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