Determination of the Optimal Operation Mode of the Platinum Dehydrogenation Catalysts / E. D. Ivanchina [et al.]

Уровень набора: (RuTPU)RU\TPU\network\4598, Advanced Materials Research : Advanced materials, synthesis, development and application, Scientific JournalАльтернативный автор-лицо: Ivanchina, E. D., chemist, Professor of Tomsk Polytechnic University, Doctor of technical sciences, 1951-, Emilia Dmitrievna;Ivashkina, E. N., chemist-technologist, Associate Professor of Tomsk Polytechnic University, Candidate of technical science, 1983-, Elena Nikolaevna;Frantsina, E. V., Chemical-technologist, Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences, 1985-, Evgeniya Vladimirovna;Silko, G. Yu., chemist, assistant of Tomsk Polytechnic University, 1990-, Galina Yurievna;Kiseleva, S.Коллективный автор (вторичный): Национальный исследовательский Томский политехнический университет (ТПУ), Институт природных ресурсов (ИПР), Кафедра химической технологии топлива и химической кибернетики (ХТТ)Язык: английский.Серия: Diagnostics and Engineering of Novel MaterialsРезюме или реферат: The main results of thermodynamic analysis and mathematical simulation of the deactivation of a platinum dehydrogenation catalyst by coke-generating compounds are presented. Developed model allows calculating the optimal flow rate of water fed to the reactor to maintain the conditions of thermodynamic equilibrium of the coke formation reaction and oxidation of intermediate condensation products with water. A comparative evaluation of different raw cycles of platinum-dehydrogenation catalysts is presented and shown to cause reduced production of the desired product was the change the composition of the feedstock..Аудитория: .Тематика: электронный ресурс | труды учёных ТПУ | кокс | формирование | дегидрирование | математические модели | катализаторы Ресурсы он-лайн:Щелкните здесь для доступа в онлайн
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The main results of thermodynamic analysis and mathematical simulation of the deactivation of a platinum dehydrogenation catalyst by coke-generating compounds are presented. Developed model allows calculating the optimal flow rate of water fed to the reactor to maintain the conditions of thermodynamic equilibrium of the coke formation reaction and oxidation of intermediate condensation products with water. A comparative evaluation of different raw cycles of platinum-dehydrogenation catalysts is presented and shown to cause reduced production of the desired product was the change the composition of the feedstock.

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