Journal issues: 4/2012
Language: (RU, EN)
1 July, 2012
Mathematical modeling fractionation stage of reactive distillation process for production of ethylene glycol
It is given fractionation stage of reactive distillation process. Rectification process is calculated by models of static on the base of conception of theoretical tray which ensure improvement of equilibrium between vapor and liquid passed in infinity time. There are examined a six version column working for receiving ethylene glycol high purify. Ethylene glycol high purify can be production only in that case when goods ethylene glycol is aside as side product from reactive distillation column. It is proved by indirect testify about adequacy of work out combined mathematical model of column.
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- Samoilov N.A., Mnushkin I.A., Mnushkina O.I. Mathematical modeling of reactive distillation column for the production of ethylene glycol, XVII International Conference on Chemical Reactors “CHEMREACTOR-17”, May 15-19, 2006, AtheneCrete, Greece. PP. 694 - 697
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adequacy of mathematical model; mathematical model; reactive distillation process; receiving ethylene glycol; rectification; theoretical tray; адекватность математической модели; математическая модель; процесс получения этиленгликоля; реакционное фракционирование; теоретическая тарелка References to this article (GOST) N.A. Samoilov, I.A. Mnushkin. Mathematical modeling fractionation stage of reactive distillation process for production of ethylene glycol // Electronic scientific journal "Oil and Gas Business". 2012. №4. P.158-164. URL: http://ogbus.ru/eng/authors/Samoilov/Samoilov_3e.pdf