Author:
Kuzevanov V S,Garyaev A B,Zakozhurnikov S S,Zakozhurnikova G S
Abstract
Abstract
A detailed analysis of heat and mass transfer processes and chemical transformations in a high-temperature gas flow with solid particles is a very difficult task. Using the phenomenological approach, the authors succeeded in obtaining a closed system of equations, the solution of which allows us to determine the main parameters of the stationary process for the production of silicon carbide. It is assumed that the implementation of two technological conditions: maintaining the required temperature level of the system “fluidizing gas - solid particles” in the production process and the continuous removal of both the final product - silicon carbide, and small unreacted particles. Variant calculations were carried out with the determination of the parameters of the continuous process for the production of fine silicon carbide, in particular, the optimal ratio of the initial sizes of carbon-containing particles and SiO2
particles and the maximum possible yield of the final product. The qualitative agreement of the calculation results with the data obtained in experiments with periodic loading of reacting components is shown.
Reference11 articles.
1. Calculation of the time of evaporation of dispersed particles;Dokhov;Fundamental research,2006
2. Fluidized-bed char combustion diffusion limited models;Bukur;Chemical Engineering Sciences,1981
3. Mathematical modeling of the process of carbidization of syntactic foams;Barabanov;Chemistry and Chemical Technology,1998
Cited by
3 articles.
订阅此论文施引文献
订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献