Research output: Contribution to journal › Article › peer-review
CO2hydrogenation to dimethyl ether over In2O3catalysts supported on aluminosilicate halloysite nanotubes. / Pechenkin, Alexey; Potemkin, Dmitry; Badmaev, Sukhe et al.
In: Green Processing and Synthesis, Vol. 10, No. 1, 01.01.2021, p. 594-605.Research output: Contribution to journal › Article › peer-review
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TY - JOUR
T1 - CO2hydrogenation to dimethyl ether over In2O3catalysts supported on aluminosilicate halloysite nanotubes
AU - Pechenkin, Alexey
AU - Potemkin, Dmitry
AU - Badmaev, Sukhe
AU - Smirnova, Ekaterina
AU - Cherednichenko, Kirill
AU - Vinokurov, Vladimir
AU - Glotov, Aleksandr
N1 - Funding Information: Funding information: This research was funded by RFBR project 19-33-60056 and as a part of the state task of Gubkin University (synthesis of MCM-41/HNT, textural properties evaluation, TEM), project number FSZE-2020-0007 (0768-2020-0007, A.G., V.V., K.Ch.). Publisher Copyright: © 2021 Alexey Pechenkin et al., published by De Gruyter.
PY - 2021/1/1
Y1 - 2021/1/1
N2 - This work presents results on CO2 hydrogenation to dimethyl ether (DME) over bifunctional catalysts consisting of In2O3, supported on natural clay halloysite nanotubes (HNT), and HNT modified with Al-MCM-41 silica arrays. The catalysts were characterized by TEM, STEM, EDX-mapping, NH3-TPD, XRD, low-temperature nitrogen adsorption, TPO, and H2-TPR techniques. Catalytic properties of In2O3/HNT and In2O3/Al-MCM-41/HNT in the CO2 hydrogenation to DME were investigated in a fixed-bed continuous flow stainless steel reactor at 10-40 atm, in the temperature range of 200-300°C, at GHSV = 12,000 h-1 and molar ratio of H2:CO2 = 3:1. The best catalyst for CO2 hydrogenation was In2O3/Al-MCM-41/HNT that provided DME production rate 0.15 gDME·(gcat·h)-1 with DME selectivity 53% and at 40 bar, GHSV = 12,000 h-1, and T = 250°C. It was shown that In2O3/Al-MCM-41/HNT exhibited stable operation for at least 40 h on stream.
AB - This work presents results on CO2 hydrogenation to dimethyl ether (DME) over bifunctional catalysts consisting of In2O3, supported on natural clay halloysite nanotubes (HNT), and HNT modified with Al-MCM-41 silica arrays. The catalysts were characterized by TEM, STEM, EDX-mapping, NH3-TPD, XRD, low-temperature nitrogen adsorption, TPO, and H2-TPR techniques. Catalytic properties of In2O3/HNT and In2O3/Al-MCM-41/HNT in the CO2 hydrogenation to DME were investigated in a fixed-bed continuous flow stainless steel reactor at 10-40 atm, in the temperature range of 200-300°C, at GHSV = 12,000 h-1 and molar ratio of H2:CO2 = 3:1. The best catalyst for CO2 hydrogenation was In2O3/Al-MCM-41/HNT that provided DME production rate 0.15 gDME·(gcat·h)-1 with DME selectivity 53% and at 40 bar, GHSV = 12,000 h-1, and T = 250°C. It was shown that In2O3/Al-MCM-41/HNT exhibited stable operation for at least 40 h on stream.
KW - COhydrogenation
KW - dimethyl ether
KW - halloysite nanotubes
KW - indium oxide catalysts
KW - mesoporous aluminosilicates
UR - http://www.scopus.com/inward/record.url?scp=85117930929&partnerID=8YFLogxK
U2 - 10.1515/gps-2021-0058
DO - 10.1515/gps-2021-0058
M3 - Article
AN - SCOPUS:85117930929
VL - 10
SP - 594
EP - 605
JO - Green Processing and Synthesis
JF - Green Processing and Synthesis
SN - 2191-9542
IS - 1
ER -
ID: 34607604