Catalytic cracking of phenolic compounds to aromatic hydrocarbons is vital to the utilization of lignin. In this work, pristine amorphous SiO2–Al2O3 was used as a catalyst to produce aromatic hydrocarbons… Click to show full abstract
Catalytic cracking of phenolic compounds to aromatic hydrocarbons is vital to the utilization of lignin. In this work, pristine amorphous SiO2–Al2O3 was used as a catalyst to produce aromatic hydrocarbons from lignin-derived phenolics by catalytic cracking using methanol as the solvent. These catalysts were characterized by various techniques (XRD, NH3-TPD, Py-IR, etc.) and evaluated on a fixed bed reactor using guaiacol as a model compound. The effects of reaction temperature, the flow of carrier gas, the molar ratio of guaiacol to methanol, and WHSV were investigated. 33-SA (SiO2–Al2O3 with the SiO2 content of 33%) exhibited the best catalytic activity due to its high content of Lewis acid sites (168.47 μmol g−1). Co-feeding with methanol promoted the removal of oxygen atoms and improved the reaction system H/Ceff. Under the optimal conditions of 400 °C, 25 mL min−1 N2, a molar ratio of methanol to guaiacol of 25, and WHSV of 8/3 h−1, the yield of aromatic hydrocarbons reached 57.93%. The deactivating species in the transformation of guaiacol into aromatic hydrocarbons on catalysts were also studied.
               
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