Parametric Optimization of a Reactive Distillation Column for the Ethyl Tert-Butyl Ether Production

Parametric Optimization of a Reactive Distillation Column for the Ethyl Tert-Butyl Ether Production

Dades bibliogràfiques
Parent link:	Periodica Polytechnica Chemical Engineering.— .— Budapest: BME Vol. 68. No. 1.— 2024.— P. 116-123
Autor principal:	Garsiya Serpas K. E. Karlos Enrike
Autor corporatiu:	National Research Tomsk Polytechnic University
Altres autors:	Samborskaya M. A. Marina Anatolievna, Mityanina O. E. Olga Evgenyevna
Sumari:	Title screen Combined processes in chemical industry are of current increasing interest, since they present a feasible solution for capital and operating expenses optimization. Multiplicities, which are specific to combined processes, cause certain control and design difficulties, thus, parametric sensitivity analysis and defining the range of existing multiplicities are the necessary part of the sustainable design and development of the combined process. Parametric and design optimization is the way of decreasing capital and operational costs. The paper discusses optimization of the design and operating parameters of an ethyl-tert-butyl ether synthesis reactive distillation column. The research aims to perform a parametric sensitivity analysis and explore existent multiple steady states of the process. The areas of multiple steady states are established, the optimal column design is developed, the optimal operation modes are determined. The procedure suggested in the study is universally applicable for design and optimization of other reactive distillation processes Текстовый файл
Publicat:	2024
Matèries:	электронный ресурс труды учёных ТПУ mathematical model optimization function parametric sensitivity reactive distillation synthesis ethyl-tert-butyl ether
Accés en línia:	https://doi.org/10.3311/PPch.22137
Format:	Electrònic Capítol de llibre
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=672407

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