Determination of the Optimal Operation Mode of the Platinum Dehydrogenation Catalysts

Bibliographic Details
Parent link:Advanced Materials Research : Advanced materials, synthesis, development and application: Scientific Journal
Vol. 880 : Prospects of Fundamental Sciences Development (PFSD-2013).— 2014.— [P. 25-31]
Corporate Author: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Other Authors: Ivanchina E. D. Emilia Dmitrievna, Ivashkina E. N. Elena Nikolaevna, Frantsina E. V. Evgeniya Vladimirovna, Silko G. Yu. Galina Yurievna, Kiseleva S.
Summary:Title screen
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.
Режим доступа: по договору с организацией-держателем ресурса
Published: 2014
Series:Diagnostics and Engineering of Novel Materials
Subjects:
Online Access:http://dx.doi.org/10.4028/www.scientific.net/AMR.880.25
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=640648

MARC

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225 1 |a Diagnostics and Engineering of Novel Materials 
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330 |a 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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701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |3 (RuTPU)RU\TPU\pers\31274 
701 1 |a Ivashkina  |b E. N.  |c Chemical Engineer  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1983-  |g Elena Nikolaevna  |y Tomsk  |3 (RuTPU)RU\TPU\pers\31275  |9 15453 
701 1 |a Frantsina  |b E. V.  |c Chemical Engineer  |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences  |f 1985-  |g Evgeniya Vladimirovna  |3 (RuTPU)RU\TPU\pers\32193  |9 16193 
701 1 |a Silko  |b G. Yu.  |c chemist  |c assistant of Tomsk Polytechnic University  |f 1990-  |g Galina Yurievna  |3 (RuTPU)RU\TPU\pers\35979  |9 19120 
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