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В. А. Кириллов

Boreskov Institute of Catalysis

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Н. А. Кузин

Novosibirsk State Technical University

А. Б. Шигаров

Boreskov Institute of Catalysis

V. A. Sobyanin

Boreskov Institute of Catalysis

П. В. Снытников

Boreskov Institute of Catalysis

В. В. Киреенков

Boreskov Institute of Catalysis

Yu. I. Amosov

Boreskov Institute of Catalysis

V. D. Belyaev

Boreskov Institute of Catalysis

Д. И. Потемкин

Novosibirsk State University

S. I. Uskov

Boreskov Institute of Catalysis

Valentin N. Parmon

Boreskov Institute of Catalysis

Cooperative Institutions

Boreskov Institute of Catalysis

Russian Academy of Sciences

Novosibirsk State University

Siberian Branch of the Russian Academy of Sciences

Novosibirsk Tuberculosis Research Institute

National Research Tomsk State University

Novosibirsk State Technical University

Gazprom (Russia)

Biomass Technology Group (Netherlands)

University of Twente

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Experimental Study of the Temperature Rise in the Frontal Layer of a Structured Porous Metal Catalyst in Air Conversion of Methane

Theoretical Foundations of Chemical Engineering (2018)

А. Б. Шигаров В. А. Кириллов Н. А. Кузин В. В. Киреенков A. S. Brayko

Exothermic reaction

Endothermic process

10.1134/s0040579518020161

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Citations (3)

Explorative catalyst screening studies on reforming of glycerol in supercritical water

The Journal of Supercritical Fluids (2012)

Joost G. van Bennekom В. А. Кириллов Yu. I. Amosov Tamara Krieger R.H. Venderbosch

Methanation

Catalytic reforming

Water-gas shift reaction

10.1016/j.supflu.2012.05.014

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Citations (25)

Mathematical Modeling of Methane Air Conversion on a Structured Porous Metal Catalyst

Theoretical Foundations of Chemical Engineering (2018)

А. Б. Шигаров В. А. Кириллов Н. А. Кузин В. В. Киреенков A. S. Braiko

Endothermic process

Exothermic reaction

Plug flow

10.1134/s0040579518030144

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Citations (3)

Approaches to Utilizing Flare Gases at Oil and Gas Fields: A Review

Catalysis in Industry (2018)

П. В. Снытников Д. И. Потемкин S. I. Uskov А. В. Курочкин В. А. Кириллов

Associated petroleum gas

Flare

Shale Gas

Shale oil extraction

10.1134/s207005041803011x

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Citations (14)

Mathematical analysis of the operating modes of a catalytic reactor for thermochemical conversion of solar energy

Geliotekhnika (1987)

V. B. Skomorokhov V. I. Anikeev В. А. Кириллов

Energy transformation

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Ni/MgO Catalysts on Structured Metal Supports for the Air Conversion of Low Alkanes into Synthesis Gas

Catalysis in Industry (2020)

В. А. Кириллов А. Б. Шигаров Н. А. Кузин В. В. Киреенков A. S. Brayko

Propane

Butane

Space velocity

Liquefied petroleum gas

10.1134/s2070050420010080

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Citations (3)

Solar thermal decomposition of hydrocarbons and carbon monoxide for the production of catalytic filamentous carbon

Chemical Engineering Science (1999)

Anton Meier В. А. Кириллов G. G. Kuvshinov Yu.I. Mogilnykh Armin Reller

Carbon fibers

10.1016/s0009-2509(98)00486-2

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Citations (37)

A Mathematical Model of Fisher-Tropsch Synthesis in a Slurry Reactor

Studies in surface science and catalysis (1998)

В. А. Кириллов V.M. Khanayev V.D. Mescheryakov С. И. Фадеев R. G. Luk'yanova

Fischer–Tropsch process

10.1016/s0167-2991(98)80423-0

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Citations (2)

Self-oscillations on a partially wetted catalyst pellet in ?-methylstyrene hydrogenation: Experiment and mathematical modeling

Theoretical Foundations of Chemical Engineering (2005)

В. А. Кириллов Igor V. Koptyug А. В. Куликов Н. А. Кузин Anna A. Lysova

Pellet

Redistribution

Exothermic reaction

Liquid phase

Oscillation (cell signaling)

10.1007/s11236-005-0024-5

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Citations (7)

Chemical heat regeneration in power plants

International Journal of Energy Research (1993)

V. I. Anikeev A. S. Bobrin V. M. Khanaev В. А. Кириллов

Cycles of gas turbine devices using liquid and gas fuels with chemical heat regeneration are considered. A thermodynamic analysis of one of these schemes was carried out using energy and enthalpy balances. The behaviour of the cycle was investigated as a function of the pressure in the chemical regenerator (Pch) and in the turbine (PT), and the temperature in the chemical catalytic regenerator (Tch). Calculations were carried out at PT ⩽ 10.0 MPa, Pch ⩽ 2.0 MPa and Tch ⩽ 600 K. As a result, it was shown that the thermal efficiency ηT of the cycle with chemical regeneration of the exhaust gases increased by about 12%. The dependences of ηT on Pch and Tch were obtained.

Chemical energy

10.1002/er.4440170402

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Citations (5)

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