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Dehydrogenation of methylbutenes to isoprene: Mathematical analysis of technology upgrade options. Part i

Lamberov A.; Urtyakov P.; Gilmanov K.; Nazarov M. (2015)

© 2015 Pleiades Publishing, Ltd. The mathematical modelling of conventional metylbutene dehydrogenation technology (performed in an adiabatic reactor) and of three versions of this process conducted in a pseudo-isothermal ...
Diffusion model of the dehydrogenation of isoamylenes into isoprene in a fixed iron-potassium catalyst bed

Egorov A.; Gilmanov K.; Lamberov A.; Urtyakov P. (2014)

© Pleiades Publishing, Ltd., 2014. © A.G. Egorov, Kh.Kh. Gilmanov, A.A. Lamberov, P.V. Urtyakov, 2014. A mathematical model is suggested for the dehydrogenation of isoamylenes into isoprene in a fixed bed of industrial, ...
Influence of hydrothermal treatment conditions on the structure and catalytic activity of alumina during the skeletal isomerization of n-butenes

Lamberov A.; Sitnikova E.; Mukhambetov I.; Zalyalieva R.; Gil'mullinb R.; Gilmanov K. (2012)

In order to obtain an efficient alumina catalyst for skeleton isomerization of n-butenes with a high catalytic activity, we study the influence of hydrothermal treatment (HTT) of alumina systems at 150- 200°C on the ...
Investigating the mechanism of the effect of cerium additives on the properties of the iron-potassium system-the active component of dehydrogenation catalysts of hydrocarbons Report 2

Lamberov A.; Gilmanov K.; Dementeva E.; Kuzmina O. (2013)

The properties of the Fe2O3-K2O and Fe2O3-K2O-CeO2 model systems with weight ratios of 80: 20 and 50: 20: 30, respectively, are studied by means of thermal, magnetic, X-ray and dispersion analysis, and low-temperature ...
Pilot tests of a new domestic ZhKD catalyst for the dehydrogenation of isoamilenes into isoprene

Lamberov A.; Dementeva E.; Kuzmina O.; Gilmanov K.; Gilmullinb R. (2012)

At the Synthetic Rubber Plant of OAO Nizhnekamskneftekhim, the dehydrogenation of isoam-ilenes into isoprene is currently performed on KDOM-08 catalysts with an insufficiently high yield of iso-prene throughout the period ...
Pilot tests of the microspherical aluminochromium KDI-M catalyst for iso-butane dehydrogenation

Lamberov A.; Egorova S.; Gilmanov K.; Kataev A.; Bekmukhamedov G. (2017)

© 2017, Pleiades Publishing, Ltd.Results from pilot tests of microspherical aluminochromium KDI-M catalyst mixed with IM-2201 in a large-scale unit (Nizhnekamskneftekhim) for iso-butane dehydrogenation are discussed. ...
Study of factors affecting the erosive wear of equipment for dehydrogenation units in fluidized beds of microspherical chromia-alumina catalysts under industrial operating conditions

Kataev A.; Lamberov A.; Egorova S.; Gilmanov K. (2014)

© Pleiades Publishing, Ltd., 2014. © A.N. Kataev, A.A. Lamberov, S.R. Egorova, Kh.Kh. Gilmanov, 2014. The main problems associated with the operation of microspherical treating-type chromia-alumina catalysts with increased ...
Upgrading the industrial process flowsheet for the dehydration of methylbutenes to isoprene. II: Analysis of plant test results and industrial implementation of the upgraded design

Lamberov A.; Gilmanov K.; Gilmullin R.; Nazarov M.; Urtyakov P.; Nekhidzha Y. (2016)

© 2016, Pleiades Publishing, Ltd.Pilot tests of technology for the dehydration of methylbutenes to isoprene are performed in a tworeactor system with an additional supply of an overheated gas into the interreactor space. ...

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Просмотр по автору "Gilmanov K."

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