Quantitative studies of the kinetics of formation of aerosols from the products of polymer pyrolysis are currently at an early stage, although the nature of this phenomenon is of interest for basic and applied research. A major reason for this situation is that the experimental technique of quantitative measurements of aerosol formation rates is applicable only to singlecomponent and binary vapors, while the products of thermal decomposition of polymers cannot be classified with these systems. Moreover, they are characterized by a rather indefinite composition.In this work, we measured for the first time the overall rate of aerosol formation through nucleation in the products of thermal decomposition of polytetrafluoroethylene.Different aspects of the thermal decomposition of polytetrafluoroethylene (PTFE) have been studied (see, e.g., [1][2][3]). PTFE is stable almost up to 300°C and softens above this temperature. Its long-term exposure to higher temperatures results in noticeable destruction; in particular, at about 800°C , the thermal decomposition of PTFE leads to the C 2 F 4 monomer in 97% yield [3].The unique properties of PTFE account for its wide practical use. The methods of depositing and studying the coatings, in which heterogeneous nucleation takes place, were briefly surveyed in [4]. No information on aerosol formation in the products of thermal decomposition of PTFE is available, although dispersed powders obtained by thermal decomposition of PTFE have found significant practical use [5].The mean rates of formation of aerosols from the products of thermal decomposition of PTFE were measured with the use of a flow diffusion chamber, whose schematic diagram was described elsewhere [6]. In our studies, the main part of the chamber was a quartz tube 140 cm long with an inner diameter of 1.2 cm. The tube was divided into sections. In the first section, a PTFE sample placed in a quartz spoon was thermally decomposed. The decomposition products were transported by an argon flow into the second section, which was designed to obtain a developed laminar gas flow. To avoid aerosol formation, the temperature in the second section was 10-20°ë higher than in the first section. The temperature variation along the section length was no more than 2 K. In the third section, the flow was cooled, which led to its supersaturation and provided conditions for aerosol generation. A decreased temperature in the range 10-80°ë was maintained in the third section by means of a liquid circulator.Currently, there is still no way to separate a complicated combination of mechanisms of nanoaerosol generation; therefore, we measured the mean nucleation rate for all possible nucleation channels. Temperatures were measured with calibrated Chromel/Alumel thermocouples. High-purity argon (99.998%) was used as a carrier gas. The volumetric flow rate of the gas through the diffusion chamber was maintained at 5.0 ± 0.2 cm 3 s -1 (under normal conditions). All aerosol experiments were performed at atmospheric pressure.The products of pyrol...