Optimization of Higher Alkanes Dehydrogenation Process under Conditions of Decreased Hydrogen Containing Gas Flow with Using Mathematical Modeling; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015

Optimization of Higher Alkanes Dehydrogenation Process under Conditions of Decreased Hydrogen Containing Gas Flow with Using Mathematical Modeling; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015

التفاصيل البيبلوغرافية
Parent link:	Procedia Engineering Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015.— 2015.— [P. 26–31]
مؤلف مشترك:	Национальный исследовательский Томский политехнический университет Институт природных ресурсов Кафедра химической технологии топлива и химической кибернетики
مؤلفون آخرون:	Ivanchina E. D. Emilia Dmitrievna, Ivashkina E. N. Elena Nikolaevna, Glik P. A., Platonov V. V., Dolganov I. M. Igor Mikhailovich
الملخص:	Title screen The article proposes the way of saving catalyst resource and increasing the efficiency of higher alkanes dehydrogenation process using mathematical model method. The study has indicated, that reducing hydrogen/feedstock molar ratio results in balance shear of alkanes dehydrogenation reaction to alkenes, which is proved by the results of pilot operating of the alkenes production unit at Ltd. KINEF and by the mathematical model calculations. The results of the prediction calculation of optimum process parameters at various hydrogen/feedstock molar ratios are presented.
اللغة:	الإنجليزية
منشور في:	2015
الموضوعات:	электронный ресурс труды учёных ТПУ катализаторы дегидрирование математические модели оптимизация водородсодержащие газы
الوصول للمادة أونلاين:	http://earchive.tpu.ru/handle/11683/36156 http://dx.doi.org/10.1016/j.proeng.2015.07.282
التنسيق:	الكتروني فصل الكتاب
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=650247

مواد مشابهة

Efficiency Improvement of the Light Gasoline Fractions Isomerization by Mathematical Modeling; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

Raising the efficiency of higher alkanes dehydrogenation process; IFOST 2012; Vol. 1
منشور في: (2012)

Calculation of the Kinetic Parameters of the Hydrofining Process of Diesel Fraction Using Mathematical Modeling; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

Performance Prediction of the Catalyst PR-81 at the Production Unit Using Mathematical Modeling Method; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

Mathematical Modeling of the Process of Catalytic Hydrodewaxing of Atmospheric Gasoil Considering the Interconnection of the Technological Scheme Devices; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

Impact Toughness of 17MnSi Pipeline Steel without and after Modification by Ultrasonic Surface Impact Treatment; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

The Way of Increasing Resource Efficiency of Naphtha Reforming Under Conditions of Catalyst Acid and Metal Activity Balance by Mathematical Modeling Method; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
منشور في: (2015)

Исследование каталитической активности катализатора дегидрирования при проведении процесса в дефиците водородсодержащего газа; Функциональные материалы: разработка, исследование, применение
حسب: Глик П. А.
منشور في: (2015)

Пути повышения эффективности использования ресурса Pt-катализатора дегидрирования при снижении кратности циркуляции водородсодержащего газа; Проблемы геологии и освоения недр; Т. 2
حسب: Платонов В. В.
منشور في: ()

Modeling the process of dehydrogenation of higher paraffins; Химия и химическая технология в XXI веке; Т. 2
حسب: Trusov A.
منشور في: (2011)

An integrated criterion of efficiency for Pt catalysts in the dehydrogenation of higher n-paraffins; Catalysis in Industry; Vol. 2, iss. 4
منشور في: (2010)

Operational analysis of the installation for olefin production with changing of hydrogen-containing gas flow; Химия и химическая технология в XXI веке; Т. 2
حسب: Glik P. A.
منشور في: (2015)

Decreasing the hydrogen-rich gas circulation ratio and service life extension of the C9-C14 alkanes dehydrogenation catalyst; Chemical Engineering Journal; Vol. 282: The XXI International Conference on Chemical Reactors CHEMREACTOR-21, 15 December 2015, Amsterdam
منشور في: (2015)

Modeling of Transalkylation Stage of Ethylbenzene Manufacturing with Zeolite-catalysts; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
منشور في: (2016)

Improving the Efficiency of Dehydrogenation Catalyst Resource while Reducing the H[2] Gas Circulation Rat; Procedia Chemistry; Vol. 10 : Chemistry and Chemical Engineering in XXI century
منشور في: (2014)

Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
منشور في: (2016)

Influence of flowrate and composition of the alkanes dehydrogenation process feedstock on by-products concentration in the linear alkylbenzene sulfonic acid manufacturing technology; Catalysis Today; Vol. 378
منشور في: (2021)

Регулирование процессов закоксовывания Pt-катализаторов процесса дегидрирования н-парафинов C10-C13 в производстве синтетических моющих средств; Известия Томского политехнического университета [Известия ТПУ]; Т. 309, № 6
منشور في: (2006)

Calculation of optimal ratios between temperature and hydrogen containing gas consumption in the catalytic dewaxing process by using the mathematical model; Химия и химическая технология в XXI веке; Т. 2
حسب: Pronevich A. Yu.
منشور في: (2015)

Application of Mathematical Modeling for Optimization of Linear Alkylbenzenes Sulphonation Modes in Film Reactor; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
منشور في: (2016)

Increasing the Efficiency of Liquid Phase Alkylation of Benzene with Propylene Using the Method of Mathematical Modeling; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
منشور في: (2016)

Определение концентрации водорода в смеси водородосодержащего газа и углеродного наноматериала; Современные техника и технологии; Т. 3
حسب: Косицын В. С. Виктор Сергеевич
منشور في: (2012)

Simulation of the catalytic hydrocarbons dehydrogenation reactor under reduced H2 pressure; Chemical Reactors (CHEMREACTOR-22)
منشور في: (2016)

Comparative analysis of catalyst operation in the process of higher paraffins dehydrogenation at different technological modes using mathematical model; Petroleum Science and Technology; Vol. 36, № 20
منشور في: (2018)

Influence of technological parameters and hydrogen-containing gas consumption on the efficiency of middle distillates hydrodesulphurization process; Petroleum Science and Technology; Vol. 37, iss. 2
منشور في: (2019)

Ethanol dehydrogenation over copper supported on carbon macrofibers; Mendeleev Communications; Vol. 27, iss. 2
منشور في: (2017)

Effect of Group Composition of the Vacuum Distillate from Heavy Kazakhstan and West Siberian Oil on the Yield of Light Fractions During the Catalytic Cracking; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
منشور في: (2016)

Kinetic studies of methanol dehydrogenation. Part I: copper-silica catalysts; Reaction Kinetics, Mechanisms and Catalysis; Vol. 120, iss. 2
حسب: Shelepova E. V. Ekaterina Vladimirovna
منشور في: (2017)

Research of the associated petroleum gas conversion into aromatic hydrocarbons on a zeolite catalyst; Химия и химическая технология в XXI веке; Т. 2
حسب: Bykova V. V.
منشور في: (2021)

Thermodynamic stability of coke-generating compounds formed on the surface of platinum dehydrogenation catalysts in their oxidation with water; Petroleum Chemistry; Vol. 53, iss. 4
منشور في: (2013)

“Dehydrogenation Kinetic Model of Heavy Paraffins”: Comments on the article by H. Jiang et al.; AIChE Journal; Vol. 65, iss. 1
منشور في: (2019)

Computer modeling system for diagnostics of the rejections causes in the working of the high paraffins dehydrogenation unit; Химия и химическая технология в XXI веке; Т. 2
حسب: Belinskaya N. S.
منشور في: (2011)

Измерение эффективной доли запаздывающих нейтронов методом α-Росси в водородсодержащих средах; Атомная энергия; Т. 100, вып. 5
حسب: Дулин В. А.
منشور في: (2006)

Анализ работы установки получения олефинов в условиях изменяющегося расхода водородсодержащего газа; Проблемы геологии и освоения недр; Т. 2
حسب: Глик П. А.
منشور في: ()

Влияние технологических условий и расхода водородсодержащего газа на эффективность процесса гидроочистки среднедистиллятных фракций; Технологии нефти и газа; № 6 (119)
منشور في: (2018)

Determination of the Optimal Operation Mode of the Platinum Dehydrogenation Catalysts; Advanced Materials Research : Advanced materials, synthesis, development and application; Vol. 880 : Prospects of Fundamental Sciences Development (PFSD-2013)
منشور في: (2014)

Механические свойства металлопроката сварных конструкций в условиях водородсодержащих сред; Техническая диагностика и неразрушающий контроль; № 1
حسب: Бернацкий А. В.
منشور في: (2004)

Cr[2]O[3]/Al-Al[2]O[3] composite catalysts for hydrocarbons dehydrogenation prepared from aluminum nanopowder; AIP Conference Proceedings; Vol. 1772 : Prospects of Fundamental Sciences Development (PFSD-2016)
منشور في: (2016)

Моделирующая система процесса каталитической депарафинизации средних дистиллятов; Химия и химическая технология в XXI веке
حسب: Афанасьева Д. А.
منشور في: (2016)

Исследование процесс а каталитического риформинга бензинов методом математического моделирования; Химия и химическая технология в XXI веке
حسب: Курская Д. А.
منشور في: (2016)