Auto-catalyzed hydrolytic depolymerization of poly(butylene terephthalate) (PBT) waste in neutral water was carried out in an autoclave at 200 , 215 , 230 , and 245 C under autogenously pressure. The effects of particle size, agitator speed, charge ratio, and reaction time on PBT hydrolyses were studied. Reaction products were terephthalic acid (TPA) and 1,4-butanediol (BD) that were recovered, analyzed, and confirmed. Yields of TPA and BD were almost equal to PBT conversion. Analyses of PBT waste samples were also undertaken. A kinetic model for PBT hydrolysis was fitted with the experimental data. Moreover, a noncatalytic PBT hydrolysis was studied to understand the effect of auto-catalyzed action during reaction. Various kinetic parameters (i.e., hydrolysis rate constant, equilibrium constant, backward rate constant, Gibbs free energy, enthalpy, and entropy) of reaction were calculated. The transfer of laboratory data is required during process commercialization through pilot plant. The dependence of the rate constant on the reaction temperature was correlated by the Arrhenius plot giving activation energy of 87 kJ=mol and the corresponding Arrhenius constant of 5.56 Â 10 9 [(g ET=mol) 1.5 min À1 ] for PBT hydrolysis.
INTRODUCTIONPoly(butylene terephthalate) (PBT) is a thermoplastic group of polyesters and it can be used for various domestic as well as industrial applications. It can be processed into fibers, spanning, high-performance technical yarns, bottles, sheets, and films. Poly(butylene terephthalate) is synthesized by step-growth polymerization between butylene glycol (BG) and TPA [1] . PBT is often synthesized by ester-exchange polymerization using weak basic catalyst [1] . PBT is produced by the reaction of dimethyl terephthalate (DMT) with BD [1] . The market for PBT is increasing rapidly and produces high PBT waste materials after use or during PBT synthesis. Ecological and economical considerations advocate the introduction of wide-scale recycling of PBT waste. Hence, among different methods of polyester recycling, chemical recycling has recently been paid much attention [2][3][4][5] . Moreover, researchers [6] have reported the process of alkali hydrolysis of PBT in various solvents, but reaction kinetic studies have not been conducted, researchers [6] have not undertaken complete recovery of value-added monomeric products from PBT, and their conversion was very low. Appreciable amounts of monomers were obtained during recycling [7,8] . A heterogeneous reaction has not been discussed for complete recovery of ethylene glycol [9] in spite of the importance of kinetic effects on polyester hydrolysis [10] . Rate constants obtained by researchers [9,10] were much lower than those reported for melt polyester hydrolysis with excess water [11] . Researchers [12] have studied polyester hydrolysis using catalyst and reported that the corresponding reaction rate constants were found to be about 20% greater than those obtained for uncatalyzed hydrolysis. However, later, other researchers [13] have reported t...