Zobrazeno 1 - 10
of 44
pro vyhledávání: '"L.L. Makarshin"'
Autor:
A. G. Gribovsky, A. S. Klimenko, D.V. Andreev, S. A. Prikhod’ko, N. Yu. Adonin, L.L. Makarshin
Publikováno v:
Kataliz v promyshlennosti. 20:40-49
The possibility to use microchannel flow reactors for obtaining kinetic and technological parameters of the synthesis of 1-butyl-3-methylimidazolium chloride (BMIMCl) ionic liquid was demonstrated for the reaction of 1-methylimidazole (MIm) with 1-ch
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a1ac9b56c8bb7545b0977707556fee04
https://doi.org/10.18412/1816-0387-2020-1-40-49
https://doi.org/10.18412/1816-0387-2020-1-40-49
Autor:
Z. P. Pai, D.V. Andreev, E. E. Sergeev, A.G. Gribovskii, L.L. Makarshin, S. A. Prikhod’ko, Valentin N. Parmon, N.Yu. Adonin
Publikováno v:
Chemical Engineering Journal. 330:899-905
Flow microchannel reactor was used to study the synthesis of iminodiacetic acid (IDA) via the catalytic oxidative dehydrogenation of diethanolamine (DEA) over catalyst Cu/ZrO2 (containing copper in amount of 10 mass%) at various residence times, reac
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::39ae374646518c9c1a10f81a4b96c337
https://doi.org/10.1016/j.cej.2017.08.028
https://doi.org/10.1016/j.cej.2017.08.028
Autor:
N.V. Vernikovskaya, E.V. Ovchinnikova, L.L. Makarshin, D.V. Andreev, A.G. Gribovskii, V. A. Chumachenko
Publikováno v:
Chemical Engineering Journal. 308:135-141
The paper deals with catalytic oxidation of methanol to formaldehyde in a microchannel reactor (MCR) in view of the process intensification. Every channel in the experimental MCR was 1 mm in diameter, 10 mm in height and was filled with an industrial
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::48b8d622da92f1b1198a8492ac65001f
https://doi.org/10.1016/j.cej.2016.09.058
https://doi.org/10.1016/j.cej.2016.09.058
Publikováno v:
Chemical Engineering Journal. 273:130-137
A thermally autonomous microchannel reactor (AMR) for production of hydrogen in the steam reforming of methanol has been designed and tested. The reactor consists of an evaporator, a stirrer, and a microchannel catalytic unit (MCU) containing a catal
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::7cdb274c4a8f85394dd4f7027332c455
https://doi.org/10.1016/j.cej.2015.03.036
https://doi.org/10.1016/j.cej.2015.03.036
Autor:
A.G. Gribovskii, Valentin N. Parmon, V.V. Privezentsev, Vladislav A. Sadykov, D.V. Andreev, L.L. Makarshin
Publikováno v:
Fuel Processing Technology. 131:21-28
Operation of a microchannel reactor during the partial oxidation of methane has been studied. Methods for the deposition of a durable (Ni–Pt)/LaCeZrO catalyst on the Fecralloy microchannel plates working under thermocycling (up to 900 °C) conditio
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::4fabf72cc319594f2db1132ea4a36ace
https://doi.org/10.1016/j.fuproc.2014.10.031
https://doi.org/10.1016/j.fuproc.2014.10.031
Autor:
E. E. Sergeev, L.L. Makarshin, Valentin N. Parmon, Elena Zhizhina, A.G. Gribovskii, D.Yu. Yushchenko, Z. P. Pai, D.V. Andreev
Publikováno v:
Chemical Engineering Journal. 259:252-256
Triethanolamine synthesis from ammonia and ethylene oxide in a continuous flow microchannel reactor has been studied in a wide range of temperatures and residence times. Microchannel reactor performance has been compared to that of conventional tubul
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ecaa41425fe86511cd5fc10a077060f3
https://doi.org/10.1016/j.cej.2014.07.118
https://doi.org/10.1016/j.cej.2014.07.118
Autor:
Natalia Mezentseva, Eugene Ivanov, Mikhail N. Simonov, D.V. Andreev, Vladislav A. Sadykov, L.L. Makarshin, Ludmilla Bobrova, Alexander Gribovskii
Publikováno v:
Catalysts, Vol 7, Iss 10, p 310 (2017)
Catalysts; Volume 7; Issue 10; Pages: 310
Catalysts; Volume 7; Issue 10; Pages: 310
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 ra
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::9c821c49ef185c3fcc04966e183a518a
https://www.mdpi.com/2073-4344/7/10/310
https://www.mdpi.com/2073-4344/7/10/310
Autor:
Valentin N. Parmon, D.V. Andreev, L.L. Makarshin, A.G. Gribovskiy, V.A. Vorontsov, V.Y. Ylianitsky
Publikováno v:
International Journal of Hydrogen Energy. 39:325-330
Partial oxidation of methane (POM) has been tested in an asymmetric microchannel reactor with different inlet configurations. One inlet of the reactor provided successive splitting of an inlet flow into parallel channels, whereas the opposite inlet a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1fff3479db2fe51f024e5da5794db019
https://doi.org/10.1016/j.ijhydene.2013.10.040
https://doi.org/10.1016/j.ijhydene.2013.10.040
Publikováno v:
Chemical Engineering Journal. 231:497-501
A new design of the multichannel reactor with a brass catalytic unit (52 mm diameter and 10 mm thick) containing 139 short channels (10 mm in length and 2 mm diameter) for the methanol steam reforming is presented. Compared to the conventional fixed-
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::9eccca85c26225040aff422c48a5d0f4
https://doi.org/10.1016/j.cej.2013.07.068
https://doi.org/10.1016/j.cej.2013.07.068
Publikováno v:
Chemical Engineering Journal. 178:276-281
Microchannel catalytic reactors have repeatedly proved their high efficiency in the process of partial oxidation of methane (POM) as compared to traditional fixed-bed catalytic reactors. However, a serious problem of the microchannel reactor operatio
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e67fc144f04951a2b2820cc98b8f31fe
https://doi.org/10.1016/j.cej.2011.10.002
https://doi.org/10.1016/j.cej.2011.10.002