Abstract
The results of calculations using the kinetic models of material balance of methane–hydrogen, propane–propylene, butylene–divinyl, and isobutylene regions were presented. Together with the previously calculated ethylene region, these regions constitute the chemical-technological complex for cracking and pyrolysis gas processing. The final scheme of the chemical-technological complex with indication of all of its inlet and outlet flows and connections between the material and recirculation flows between regions was presented. The production capacities of reactor elements were determined for all the desired products of the chemical-technological complex.
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