Crude Oil Distillation with Superheated Water Steam: Parametrical Sensitivity and Optimization

Crude Oil Distillation with Superheated Water Steam: Parametrical Sensitivity and Optimization

Dades bibliogràfiques
Parent link:	Procedia Chemistry Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 337-342]
Altres autors:	Samborskaya M. A. Marina Anatolievna, Gusev V. P. Valeriy Petrovich, Gryaznova I. A. Inga Andreevna, Vdovushkina N. S., Wolf A. V. Andrey Viktorovich
Sumari:	Title screen Stability of crude oil distillation units was analyzed with mathematical models developed using Aspen Hysys. Parametrical sensitivities of light fractions yields, heat duties and steam load of column trays to perturbations of superheated steam flow rate were estimated. Objective function based on the light products yields and energy consumption for distillation was formed. The maxima of the objective function were calculated depending on operational parameters and flow rate of water steam. Режим доступа: по договору с организацией-держателем ресурса
Idioma:	anglès
Publicat:	2014
Matèries:	электронный ресурс труды учёных ТПУ перегонка сырая нефть параметрическая чувствительность оптимизация целевые функции водяные пары crude oil distillation unit superheated water steam parametrical sensitivity optimization objective function
Accés en línia:	http://dx.doi.org/10.1016/j.proche.2014.10.057 http://earchive.tpu.ru/handle/11683/35517
Format:	Electrònic Capítol de llibre
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639519

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