Crude Oil Distillation with Superheated Water Steam: Parametrical Sensitivity and Optimization; Procedia Chemistry; Vol. 10 : Chemistry and Chemical Engineering in XXI century
| Parent link: | Procedia Chemistry Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 337-342] |
|---|---|
| Corporate Authors: | Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ), Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра общей химической технологии (ОХТ) |
| Outros autores: | Samborskaya M. A. Marina Anatolievna, Gusev V. P. Valeriy Petrovich, Gryaznova I. A. Inga Andreevna, Vdovushkina N. S., Wolf A. V. Andrey Viktorovich |
| Summary: | 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: | inglés |
| Publicado: |
2014
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| Subjects: | |
| Acceso en liña: | http://dx.doi.org/10.1016/j.proche.2014.10.057 http://earchive.tpu.ru/handle/11683/35517 |
| Formato: | MixedMaterials Electrónico Capítulo de libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639519 |
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