Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes / V. A. Chuzlov, N. V. Chekantsev, E. D. Ivanchina
Уровень набора: (RuTPU)RU\TPU\network\3889, Procedia ChemistryЯзык: английский.Резюме или реферат: The technique of developing a mathematical model of catalytic isomerization of light naphtha is stated Using experimental data from an industrial isomerization unit shows adequacy of the mathematical model to the real process. The paper presents a method for optimizing the operation of the plant together with catalytic isomerization unit and separation columns. Selection of optimal modes of separation columns allows achieving the desired flow separation between units, as well as extension of the life of the catalyst SI-2..Примечания о наличии в документе библиографии/указателя: [References: р. 242-243 (12 tit.)].Аудитория: .Тематика: электронный ресурс | труды учёных ТПУ | математические модели | изомеризация | моделирование | реакторы | колонки | катализаторы | rectification | isomerization | simulation | reactor | column Ресурсы он-лайн:Щелкните здесь для доступа в онлайн | Щелкните здесь для доступа в онлайнНет реальных экземпляров для этой записи
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[References: р. 242-243 (12 tit.)]
The technique of developing a mathematical model of catalytic isomerization of light naphtha is stated Using experimental data from an industrial isomerization unit shows adequacy of the mathematical model to the real process. The paper presents a method for optimizing the operation of the plant together with catalytic isomerization unit and separation columns. Selection of optimal modes of separation columns allows achieving the desired flow separation between units, as well as extension of the life of the catalyst SI-2.
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