Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6584035 | Chemical Engineering Journal | 2015 | 12 Pages |
Abstract
In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
E.D. Ivanchina, M.V. Kirgina, N.V. Chekantsev, B.V. Sakhnevich, E.V. Sviridova, R.V. Romanovskiy,