Free radical polymerization kinetics of diallyl terephthalate in bulk was investigated in a wide temperature range from 50degreesC to 150degreesC with four different peroxide initiators. Conversion points were measured using Fourier Transform Infrared (FTIR) measurements. The initiator efficiencies and the initiator decomposition rate constants were evaluated from special experiments, applying the theory of dead end polymerization. In addition, the ratios between the degradative and the effective kinetic rate constants to propagation rate constants were obtained from molecular weight measurements at various initiator concentrations. The ratio of chemically controlled termination and propagation rate constant k(pc)(2) /k(tc) of the polymerization system was PC obtained using the initial rates of polymerization and the number average molecular weight data between 0.25 (.) 10(-3) and 15.7 (.) 10(-3) L mol(-1) s(-1). The glass transition temperature of the polymer, 191degreesC, was measured by the Alternating Differential Scanning Calorimetry (ADSC) technique. Computed conversions from the developed kinetic model were in good agreement with the conversion and molecular weight measured data. The values of diffusion controlled propagation and termination rate constants k(td0) and k(pd0) with clear and physical meaning were the only two parameters obtained from the developed kinetic model fitting. (C) 2004 Society of Plastics Engineers.