Yury Yu Kosivtsov

Prof. Yury Yu Kosivtsov

Tver State Technical University, Tver', Russia
orcid

Research Focus & Metrics

Academic Career Length

28Years (1999-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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27 March 2023 in Catalysts
Verified
Journal Article
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ASAntonina A. Stepacheva
Antonina A. Stepacheva
MMMariia E. Markova
Mariia E. Markova
YLYury Vladimirovich Lugovoy
Yury Vladimirovich Lugovoy
YKYury Yu Kosivtsov
Yury Yu Kosivtsov
VMValentina Matveeva
Valentina Matveeva
MSMikhail G. Sulman
Mikhail G. Sulman
Carbon materials are widely used in catalysis as effective catalyst supports. Carbon supports can be produced from coal, organic precursors, biomass, and polymer wastes. Biomass is one of the promising sources used to produce carbon-based materials with a high surface area and a hierarchical structure. In this review, we briefly discuss the methods of biomass-derived carbon supported catalyst preparation and their application in biodiesel production, organic synthesis reactions, and electrocatalysis.

1 November 2009 in Chemical Engineering Journal
Verified
Journal Article
Closed access
MSMikhail G. Sulman
Mikhail G. Sulman
YKYury Yu Kosivtsov
Yury Yu Kosivtsov
ESE. Sulman
E. Sulman
VAV. Alfyorov
V. Alfyorov
YLYury Vladimirovich Lugovoy
Yury Vladimirovich Lugovoy
Dmitry MurzinDmitry Murzin
Dmitry Murzin

1 October 1999 in Journal of Molecular Catalysis A: Chemical
Verified
Journal Article
Closed access
ESE Sulman
E Sulman
VMV Matveeva
V Matveeva
AUA Usanov
A Usanov
YKYury Yu Kosivtsov
Yury Yu Kosivtsov
GDG Demidenko
G Demidenko
PVP Valetsky
P Valetsky

1 November 2007 in Chemical Engineering Journal
Verified
Journal Article
Closed access
ESE.M. Sulman
E.M. Sulman
VAV.V. Alferov
V.V. Alferov
YKYury Yu Kosivtsov
Yury Yu Kosivtsov
ASA.I. Sidorov
A.I. Sidorov
OMO.S. Misnikov
O.S. Misnikov
Dmitry MurzinDmitry Murzin
Dmitry Murzin

1 February 2014 in Chemical Engineering Journal
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Journal Article
Closed access
KCK.V. Chalov
K.V. Chalov
YLYury Vladimirovich Lugovoy
Yury Vladimirovich Lugovoy
Valentin Yu DoludaValentin Yu Doluda
Valentin Yu Doluda
ASA.I. Sidorov
A.I. Sidorov
MSM.G. Sulman
M.G. Sulman
MSMikhail G. Sulman
Mikhail G. Sulman

2 December 2023 in Catalysts
Verified
Journal Article
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Valery TarabankoValery Tarabanko
Valery Tarabanko
KKKonstantin Kaigorodov
Konstantin Kaigorodov
Aleksandr KazachenkoAleksandr Kazachenko
Aleksandr Kazachenko
Marina A. SmirnovaMarina A. Smirnova
Marina A. Smirnova
YCYulia V. Chelbina
Yulia V. Chelbina
VGViktor Alexandrovich Golubkov
Viktor Alexandrovich Golubkov
The influence of mass transfer intensity on the kinetics of the catalytic oxidation of flax shives with oxygen in alkaline media to aromatic aldehydes and pulp was studied. The process was carried out in two autoclaves, with moderate stirring (stirrer engine of 8 W) and intense stirring (stirrer engine of 200 W). The oxidation of flax shives into vanillin, syringaldehyde, and pulp was shown to proceed as a completely diffusion-controlled process under the studied conditions, both moderate and intense stirring. Depending on the process conditions, it can be limited by stages of oxygen transfer through the diffusion boundary layer near the gas–liquid interface (low intensity of mass transfer) as well as by reagents’ inner diffusion in the porous and solid matter of the flax shive particle (high intensity of mass transfer). The results on the influence of the stirring speed and volume of the reaction mass on the rates of oxygen consumption and vanillin accumulation were obtained. They were described using a known simple model connecting the intensity of mass transfer and the stirring power density in the bulk of the liquid phase in terms of algebra equations.