This research aims to develop a liquid–solid–liquid phase-transfer catalyst (PTC) catalytic kinetic model of carboxylate esterification unpublished previously. The bimolecular nucleophilic substitution reaction of sodium benzoate with benzyl bromide has been experimented with the immobilized solid PTC to propose the kinetic model and calculate the apparent reaction rate constant and activation energy. We proposed the proper kinetic model of the esterification successfully. In addition, the experimental results comprehensively matched the pseudo-first-order reaction formula. Under the multiple steps of recovery, reuse, and regeneration, the structure of tri-phase PTC support remains well, nor will it destroy the activated site immobilized on the support. Comparing the reactivity of the fresh PTC with PTCs recovered four times, the reactivity does not decrease with the continued recovery, indicating excellent catalytic reactivity. Besides, the esterification, etherification, and benzylation reactions catalyzed by regenerated PTCs and their yields are not much different from those of the original fresh PTCs. It shows that the catalytic activity of regenerated PTC is quite excellent. In our opinion, exploring the regeneration and reduction of PTC can reduce cost, save resources, possesses the potential to apply to other reaction systems, and improve conventional production.
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