<HashMap><database>biostudies-literature</database><scores/><additional><omics_type>Unknown</omics_type><volume>13(16)</volume><submitter>Zhang D</submitter><pubmed_abstract>Catalytic cracking of phenolic compounds to aromatic hydrocarbons is vital to the utilization of lignin. In this work, pristine amorphous SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> 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, NH&lt;sub>3&lt;/sub>-TPD, Py-IR, &lt;i>etc.&lt;/i>) 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 (SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> with the SiO&lt;sub>2&lt;/sub> content of 33%) exhibited the best catalytic activity due to its high content of Lewis acid sites (168.47 μmol g&lt;sup>-1&lt;/sup>). Co-feeding with methanol promoted the removal of oxygen atoms and improved the reaction system H/C&lt;sub>eff&lt;/sub>. Under the optimal conditions of 400 °C, 25 mL min&lt;sup>-1&lt;/sup> N&lt;sub>2&lt;/sub>, a molar ratio of methanol to guaiacol of 25, and WHSV of 8/3 h&lt;sup>-1&lt;/sup>, the yield of aromatic hydrocarbons reached 57.93%. The deactivating species in the transformation of guaiacol into aromatic hydrocarbons on catalysts were also studied.</pubmed_abstract><journal>RSC advances</journal><pagination>10830-10839</pagination><full_dataset_link>https://www.ebi.ac.uk/biostudies/studies/S-EPMC10074442</full_dataset_link><repository>biostudies-literature</repository><pubmed_title>Production of aromatic hydrocarbons from lignin derivatives by catalytic cracking over a SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> catalyst.</pubmed_title><pmcid>PMC10074442</pmcid><pubmed_authors>Yin H</pubmed_authors><pubmed_authors>Zhang D</pubmed_authors><pubmed_authors>Ma L</pubmed_authors><pubmed_authors>Li S</pubmed_authors><pubmed_authors>Zhang Y</pubmed_authors><pubmed_authors>Zhang X</pubmed_authors><pubmed_authors>Zheng Q</pubmed_authors><pubmed_authors>Fu P</pubmed_authors></additional><is_claimable>false</is_claimable><name>Production of aromatic hydrocarbons from lignin derivatives by catalytic cracking over a SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> catalyst.</name><description>Catalytic cracking of phenolic compounds to aromatic hydrocarbons is vital to the utilization of lignin. In this work, pristine amorphous SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> 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, NH&lt;sub>3&lt;/sub>-TPD, Py-IR, &lt;i>etc.&lt;/i>) 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 (SiO&lt;sub>2&lt;/sub>-Al&lt;sub>2&lt;/sub>O&lt;sub>3&lt;/sub> with the SiO&lt;sub>2&lt;/sub> content of 33%) exhibited the best catalytic activity due to its high content of Lewis acid sites (168.47 μmol g&lt;sup>-1&lt;/sup>). Co-feeding with methanol promoted the removal of oxygen atoms and improved the reaction system H/C&lt;sub>eff&lt;/sub>. Under the optimal conditions of 400 °C, 25 mL min&lt;sup>-1&lt;/sup> N&lt;sub>2&lt;/sub>, a molar ratio of methanol to guaiacol of 25, and WHSV of 8/3 h&lt;sup>-1&lt;/sup>, the yield of aromatic hydrocarbons reached 57.93%. The deactivating species in the transformation of guaiacol into aromatic hydrocarbons on catalysts were also studied.</description><dates><release>2023-01-01T00:00:00Z</release><publication>2023 Apr</publication><modification>2025-04-19T17:30:28.259Z</modification><creation>2025-04-19T17:30:28.259Z</creation></dates><accession>S-EPMC10074442</accession><cross_references><pubmed>37033419</pubmed><doi>10.1039/d3ra00990d</doi></cross_references></HashMap>