Please use this identifier to cite or link to this item: http://earchive.tpu.ru/handle/11683/35501
Title: Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes
Authors: Chuzlov, Vyacheslav Alekseevich
Chekantsev, Nikita Vitalievich
Ivanchina, Emilia Dmitrievna
Keywords: математические модели; изомеризация; моделирование; реакторы; колонки; катализаторы; rectification; isomerization; simulation; reactor; column
Issue Date: 2014
Publisher: Elsevier
Citation: Chuzlov, Vyacheslav Alekseevich. Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes [Electronic resource] / V. A. Chuzlov, N. V. Chekantsev, E. D. Ivanchina // Procedia Chemistry . — 2014 . — Vol. 10 : Chemistry and Chemical Engineering in XXI century . — [P. 236-243] .
Abstract: 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.
URI: http://earchive.tpu.ru/handle/11683/35501
Appears in Collections:Материалы конференций

Files in This Item:
File SizeFormat 
dx.doi.org-10.1016-j.proche.2014.10.040.pdf478,15 kBAdobe PDFView/Open


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.