lodoxybenzoic acid has been covalently attached to polystyrene-co-divinylbenzene beads at different capacities and the hydroquinone oxidation kinetics have been studied in a stirred batch reactor. An initial rate analysis yielded a first order dependence on the concentration of the substrate hydroquinone and the supported IBX reagent implying chemical reaction is rate limiting. An observed second order rate constant of 1.3 (+/-0.3) M-1 s(-1) was obtained for the initial rate of oxidation using the supported reagent. The activation energy was halved at later stages of reaction (greater than 50% conversion of the reagent), suggesting that intraparticle diffusion then become rate limiting as the conversion of the reagent in the bead proceeded. Unreacted shrinking core and pseudo-homogeneous diffusion-reaction models have been used to analyse the experimental data to yield values for the effective diffusivity of hydroquinone in the polymer matrix of (1.0-1.2) x 10(-11) m(2)/s. The performance of the supported reagent in a packed bed has also been studied by continuous flow of a solution of hydroquinone. The product quinone concentration profile at the reactor exit showed limited dependence on the flow-rates studied. Pronounced tailing of the product concentration was obtained for more highly loaded beads, which was attributed to hindered diffusion limiting access to the residual reactive sites.
- polymer-supported reagents
- packed bed
Jegasothy, S., Slater, N. K. H., Denecker, C., Sherrington, D. C., Lei, Z., & Sutherland, A. J. (2004). Kinetics of oxidation of hydroquinone by polymer-supported hypervalent iodine oxidant, iodoxybenzoic acid. Chemical Engineering Journal, 105(1-2), 1-10. https://doi.org/10.1016/j.cej.2004.09.004