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The process of nanocarbon of methane from methane was carried out in the presence of (CuO)x*(CoO)y*(NiO)z*(Fe2O3)k*(MoO3)m/HSZ catalyst: The essence of the method is the interaction of nitrate mixtures of metals included in the catalyst and the organic matter in the air at temperatures ≥500 ℃. The reaction is followed by the formation of finely dispersed oxides of metals. It allows calculating the concentration of system components not only at the outlet of the apparatus, but also along the length of the reactor. As a result, the methane supplied to the surface of the catalyst manages to interact with it before methane escapes with a stream of the initial gas mixture. The kinetic curves of the time dependence of the change in the specific amount of carbon in the catalyst do not have an induction period at all. The process temperature did not change and was 650 ℃. Thus, real experiments were repeated using computer technology. The peculiarity of the nanocarbon production process is that the catalyst is consumed during the process.
reactor, catalyst, methane, nanocarbon, modeling, optimization
reactor, catalyst, methane, nanocarbon, modeling, optimization
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