CO2 capture and utilization are usually done in separate unit operations. Using laser-induced pyrolysis, we transformed a mixed matrix polyimide gas separation membrane into a cathode capable of separating carbon dioxide from gas mixtu...
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Bio‐Based Phenol from Cashew Nutshells by Catalytic Hydrocardanol Trans‐Alkylation Using H‐ZSM‐5 Zeolite
Von Wiley-VCH zur Verfügung gestellt
An efficient reaction process for bio-based phenol production is developed using hydrocardanol, a saturated long-chain alkylphenol derived from agricultural waste (cashew nut shells), via H-ZSM-5-catalyzed trans-alkylation with toluene using a fixed-bed flow reactor, achieving an impressive phenol yield (>95%) with an excellent carbon balance (>99%).
Cardanol, an unsaturated long-chain alkylphenol derived from agricultural waste, has potential as a sustainable substrate for bio-based phenol production. Herein, the potential of hydrocardanol, readily obtained through cardanol hydrogenation, is demonstrated as a viable feedstock for phenol production via trans-alkylation using toluene as the alkyl acceptor. H-ZSM-5 (SiO2/Al2O3 molar ratio = 80) exhibits a 53.7% phenol yield with a high phenolics balance (86.7%) from a 10 wt% hydrocardanol solution at full conversion in a batch reactor. In contrast, cardanol gives only 27.1% phenol under the same reaction conditions. This improved yield with hydrocardanol is attributed to suppressed formation of bi- and/or polycyclic phenols via self-alkylation, due to the higher thermal stability of the saturated side chain. Realkylation of the desired phenol product largely limits the phenol yield. The model reaction experiments with phenol and 1-pentadecene show that the reaction proceeds via hydrocardanol dealkylation on the zeolite, followed by rapid isomerization, cracking and oligomerization reactions of the resulting long-chain olefin, and realkylation of toluene and phenol. This indicates that phenol alkylation could be suppressed by reducing the hydrocardanol-to-toluene ratio. This approach is validated in a fixed-bed flow reactor, achieving a high phenol yield (>95%) with a high carbon balance (>99%).
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