The thermal polymerization of inhibited styrene monomer is investigated by Accelerating Rate Calorimetry (ARC). The time-temperature-pressure data generated by this technique are utilized in evaluating the thermal hazards associated with the industrial processing of styrene monomer. Several examples are given on the interpretation and application of ARC data to environments ranging from lab to plant-scale conditions including discussions concerning the similarities and dissimilarities between the ARC and large-scale equipment. The polymerization of styrene monomer is also used to evaluate the performance of the ARC over a broad temperature range, 80-300 ~ The data indicate that removal of the radiant heater assembly yields better agreement between the heat of polymerization of styrene as measured by the ARC and corresponding values from the literature. This effect is believed to be observable only under conditions of low reaction rates for long periods of time such as in the case of styrene monomer.The evaluation of thermal and pressure hazards associated with the manufacture, transport, and storage of chemicals is an important area of research in the chemical industry. The engineering design of equipment to prevent, control or withstand runaway reactions which result in pressure increase is of great concern from a safety and loss point of view. In order to design a piece of equipment which will operate safely during an emergency situation, it is necessary to have data on the kinetics, thermodynamics, and physical properties of the potential runaway reaction.Several approaches have been utilized in the past to obtain information on the kinetics of exothermic reactions. One of the most commonly used techniques in thermal hazard evaluation is differential scanning calorimetry (DSC) which can yield both the heat of reaction and the kinetics of the reaction of interest [1 ]. A modification of the sample container used in DSC has been developed to handle volatile chemicals or materials which generate gaseous products on decomposition, conditions which are common in the chemical industry [2]. However, one limitation to the DSC methods for hazard evaluation is the difference in experimental conditions compared to normal operating conditions in a chemical plant. DSC data are obtained at a fixed heating rate which forces the reaction to occur at higher temperatures in the DSC than would be experienced during processing or storage. As a result, the experimental data often must be extrapolated to normal