Hydrodeoxygenation of Phenolic Compounds and Lignin Bio-Oil Surrogate Mixture over Ni/BEA Zeolite Catalyst and Investigation of Its Deactivation

被引:0
作者
Margellou, Antigoni G. [1 ]
Zormpa, Foteini F. [1 ]
Karfaridis, Dimitrios [2 ]
Karakoulia, Stamatia A. [3 ]
Triantafyllidis, Konstantinos S. [1 ,4 ,5 ,6 ]
机构
[1] Aristotle Univ Thessaloniki, Dept Chem, Thessaloniki 54124, Greece
[2] Aristotle Univ Thessaloniki, Dept Phys, Thessaloniki 54124, Greece
[3] Ctr Res & Technol Hellas, Chem Proc & Energy Resources Inst, Thessaloniki 57001, Greece
[4] King Fahd Univ Petr & Minerals, Dept Chem, Dhahran 31261, Saudi Arabia
[5] King Fahd Univ Petr & Minerals, Interdisciplinary Res Ctr Refining & Adv Chem, Dhahran 31261, Saudi Arabia
[6] KST, Riyadh, Saudi Arabia
基金
欧盟地平线“2020”;
关键词
lignin fast-pyrolysis bio-oil; surrogate mixture; phenolic compounds; hydrodeoxygenation; cycloalkanes; sustainable aviation and road fuels; Ni/BEA zeolite; deactivation; ACIDIC CHARACTERISTICS; DEALUMINATION METHOD; CFD SIMULATIONS; MODEL COMPOUNDS; METAL; BIOMASS; GUAIACOL; CONVERSION; SUPPORT; ANISOLE;
D O I
10.3390/catal15010048
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
Lignin is one of the main structural components of lignocellulosic biomass and can be utilized to produce phenolic compounds that can be converted downstream to cycloalkanes and aromatics, which are useful as drop-in road or aviation biofuels. Within this study, the hydrodeoxygenation of model phenolic/aromatic compounds and surrogate mixture simulating the light fraction of lignin fast-pyrolysis bio-oil was performed under mild reaction conditions. Ni/BEA zeolite was selected as a catalyst to investigate the conversion and the product selectivity of alkyl phenols (phenol, catechol, cresols), methoxy-phenols (guaiacol, syringol, creosol), aromatics (anisole, 1,2,3-trimethoxybenzene) and dimer (2-phenoxy-1-phenyl ethanol) compounds towards (alkyl)cycloalkanes. The hydrodeoxygenation of a surrogate mixture of eleven phenolic and aromatic compounds was then studied by investigating the effect of reaction conditions (temperature, time, H2 pressure, surrogate mixture concentration, and catalyst-to-feed ratio). The conversion of model compounds was in the range of 80-100%, towards a 37-81% (alkyl)cycloalkane yield, being strongly dependent on the complexity/side-chain group of the phenolic/aromatic ring. Regarding the hydrodeoxygenation of the surrogate mixture, 59-100% conversion was achieved, with up to a 72% yield of C6-C9 cycloalkanes. Characterization of spent catalysts showed that the hydrodeoxygenation of surrogate mixture led to carbonaceous depositions on the catalyst, which can be limited under lower temperatures and longer reaction conditions, while after regeneration, the physicochemical properties of catalysts can be partially recovered.
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页数:26
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