L. L. Makarshin
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Research Interests
L. L. Makarshin has a total of 8 co-authors. Here are the top co-authors by number of shared publications:
- Alexander Gribovskii
Russian Academy of Sciences
1 shared publication - Dmitry Andreev
Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk, Russia
1 shared publication - Eugene Ivanov
Boreskov Institute of Catalysis, Prospekt Akademika Lavrentieva, 5, 630090 Novosibirsk, Russia
1 shared publication - Ludmilla Bobrova
Federal Research Center Boreskov Institute of Catalysis SB RAS, 630090 Novosibirsk, Russia
1 shared publication - Mikhail N. Simonov
Department of Heterogeneous Catalysis, Boreskov Institute of Catalysis, 630090 Novosibirsk, Russia
1 shared publication - Natalia Mezentseva
Department of Heterogeneous Catalysis, Boreskov Institute of Catalysis, 630090 Novosibirsk, Russia
1 shared publication
Latest Publications
- Open Access
Water–Gas Shift Reaction over Ni/CeO2 Catalysts
This paper reports the results of a study of a water–gas shift reaction over nickel–ceria catalysts with different metal loading. Within this study, the overall CO conversion and observed kinetic behavior were investigated over the temperature range of 250–550 °C in different reactor configurations (fixed-bed and microchannel reactors). The quasi-steady state kinetics of the CO water–gas shift reaction was studied for fractions of Ni-containing cerium oxide catalysts in fixed-bed experiments at lab-scale level using a very dilute gas (1% CO + 1.8% H2O in Не). A set of experiments with a microchannel reactor was performed using the feed composition (CO:H2O:H2:N2 = 1:2:2:2), representing a product gas from methane partial oxidation. The results were interpreted using computational models. The kinetic parameters were determined by regression analysis, while mechanistic aspects were considered only briefly. Simulation of the WGS reaction in the microreactor was also carried out by using the COMSOL Multiphysics program.
Open AccessWater–Gas Shift Reaction over Ni/CeO2 Catalysts
This paper reports the results of a study of a water–gas shift reaction over nickel–ceria catalysts with different metal loading. Within this study, the overall CO conversion and observed kinetic behavior were investigated over the temperature range of 250–550 °C in different reactor configurations (fixed-bed and microchannel reactors). The quasi-steady state kinetics of the CO water–gas shift reaction was studied for fractions of Ni-containing cerium oxide catalysts in fixed-bed experiments at lab-scale level using a very dilute gas (1% CO + 1.8% H2O in Не). A set of experiments with a microchannel reactor was performed using the feed composition (CO:H2O:H2:N2 = 1:2:2:2), representing a product gas from methane partial oxidation. The results were interpreted using computational models. The kinetic parameters were determined by regression analysis, while mechanistic aspects were considered only briefly. Simulation of the WGS reaction in the microreactor was also carried out by using the COMSOL Multiphysics program.
- 1 March 2012
- Published by Pleiades Publishing Ltd in Catalysis in Industry
- Vol. 4 (1) , 27-38
Microchannel catalytic systems for the intensification of hydrogen production from carbon-containing feedstocks
- 1 March 2012
- Published by Pleiades Publishing Ltd in Catalysis in Industry
- Vol. 4 (1) , 27-38
Microchannel catalytic systems for the intensification of hydrogen production from carbon-containing feedstocks