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D

D.V. Andreev

Researcher at Russian Academy of Sciences

Publications -  29
Citations -  297

D.V. Andreev is an academic researcher from Russian Academy of Sciences. The author has contributed to research in topics: Microreactor & Hydrogen production. The author has an hindex of 9, co-authored 17 publications receiving 239 citations.

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Catalytic reactors with hydrogen membrane separation

TL;DR: In this article, the main catalytic hydrogen generation processes efficiently utilizing hydrogen-permeable membranes are described, and different membranes for hydrogen separation from gas mixtures and preparation methods are considered.
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Thermally autonomous microchannel reactor to produce hydrogen in steam reforming of methanol

TL;DR: In this article, a thermally autonomous microchannel this article for hydrogen production in the steam reforming of methanol has been designed and tested, which consists of an evaporator, a stirrer, and a microchannel catalytic unit (MCU) containing a catalyst deposited in short channels.
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Syngas production by partial oxidation of methane in a microchannel reactor over a Ni–Pt/La0.2Zr0.4Ce0.4Ox catalyst

TL;DR: In this article, an operation of a microchannel reactor during the partial oxidation of methane has been studied and the deposition of a durable (Ni-Pt)/LaCeZrO catalyst on the Fecralloy microchannel plates working under thermocycling (up to 900°C) conditions up was developed.
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Water–Gas Shift Reaction over Ni/CeO2 Catalysts

Abstract: 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.
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Microchannel reactor for intensifying oxidation of methanol to formaldehyde over Fe-Mo catalyst

TL;DR: In this paper, a micro-channel reaction for catalytic oxidation of methanol to formaldehyde in a microchannel reactor (MCR) in view of the process intensification was investigated.