To address the challenge of green recycling of carbon-fiber-reinforced polymer composites (CFRPs) imposed by highly crosslinked epoxy matrices, this study investigates peracetic-acid (PAA) oxidative degradation of a cured epoxy resin (cEP) based on diglycidyl ether of bisphenol A cured with 4,4′-diaminodiphenylmethane. Under representative conditions, PAA removes 99.8% of the epoxy matrix from CFRP laminates while retaining about 95% of the original single-filament tensile strength. To elucidate the controlling mechanisms and enable process optimization, a factorial evaluation of stirring speed, solid–liquid ratio, and temperature was performed using cEP particles as a model system. Guided by the experimentally observed “swollen reactive shell–unreacted core” morphology, a coupled swelling–intraparticle diffusion–chemical reaction–oxidant self-decay kinetic model was developed to quantitatively predict both cEP degradation and the time evolution of liquid-phase PAA concentration. Parameter estimation yields an apparent activation energy of 148.92 kJ·mol−1 for PAA-driven cEP oxidation. Although increasing temperature accelerates degradation, it also intensifies oxidant self-decay and non-productive oxidation of liquid-phase intermediates. Model-guided operation shows that stepwise PAA feeding can suppress non-target consumption and improve terminal conversion. At 353 K, using only 1.025 times the theoretical PAA requirement, stepwise feeding raises the resin degradation degree from 0.93 (single-shot) to 0.99 within 3 h, thereby minimizing oxidant cost. The demonstrated laminate-scale feasibility, together with the particle-scale kinetic framework, provides a quantitative basis for designing PAA-based CFRP recycling processes that balance resin removal, fiber integrity, and oxidant efficiency.
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