Optimization of the operation of the chemical-technological system as a whole is possible only if the efficiency of each of the associated processes of all stages of production is increased, taking into account their interrelationship. These problems are successfully solved using the methods of mathematical modeling and computer modeling systems that take into account the volatility of the raw material composition, the change in catalyst activity and a large number of control parameters. This approach was used for benzene alkylation process and allowed us to reveal regularieties of alkylation reactor depending on the technologiscal conditions in the conjugate apparatuses. Thus, optomal HF-catalyst activity depends signifacantly both on the dehydrogenation feedstock composition and its flow rate.
|Журнал||Petroleum and Coal|
|Состояние||Опубликовано - 2018|
ASJC Scopus subject areas