Mathematical modeling and steady states multiplicity analysis of methyl tert-butyl ether reactive distillation synthesis; Petroleum and Coal; Vol. 58, iss. 4

Mathematical modeling and steady states multiplicity analysis of methyl tert-butyl ether reactive distillation synthesis; Petroleum and Coal; Vol. 58, iss. 4

التفاصيل البيبلوغرافية
Parent link:Petroleum and Coal
Vol. 58, iss. 4.— 2016.— [P. 490-498]
المؤلف الرئيسي: Mityanina O. E. Olga Evgenyevna
مؤلف مشترك: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
مؤلفون آخرون: Samborskaya M. A. Marina Anatolievna, Sabiev A. N. Ayan Nurlanovich
الملخص:Title screen
The paper is devoted to a new approach to steady state multiplicity analysis of methyl tert-butyl ether (MTBE) production by means of reactive distillation. Reactive distillation systems are characterized by input and output multiplicities, which may cause complex and unpredictable behavior of the process. The fundamental mathematical model, which enables to reveal potential sources of nonlinearity of the process, is proposed. As the result of input multiplicity analysis, intervals of one steady state were found for vapor and reflux ratio. Output multiplicity analysis showed three possible steady states in the reactive section of the column, one of which is corresponded to the maximal product yield. The advantage of the method is the ability to find “input-output” multiplicities on every stage of the column by using control parameters of the feed, reboiler and condenser only.
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اللغة:الإنجليزية
منشور في: 2016
الموضوعات:
электронный ресурс
труды учёных ТПУ
дестилляция
третбутиловый спирт
математическое моделирование
анализ устойчивости
стационарное состояние
الوصول للمادة أونلاين:http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_4_2016_mytyanina_452.pdf
التنسيق: الكتروني فصل الكتاب
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652443

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