Bulletin of the Chemical Society of Japan p. 2520 - 2525 (1992)
Update date:2022-08-11
Topics:
Okabe, Kiyomi
Sayama, Kazuhiro
Matsubayashi, Nobuyuki
Shimomura, Kin'ya
Arakawa, Hironori
Hydrogenation of CO2 to methanol was carried out on Cu-ZnO/SiO2 catalysts at 493 K and 3 MPa with a flow rate of 100 cm3min-1 (H2/CO2=2).Higher selectivity (>90percent) was observed on the catalysts prepared by the alkoxide method than on a conventional catalyst prepared by the impregnation method.The selectivity was higher on the catalysts pretreated with H2 at a higher temperature, except at 873 K.The activity of the catalyst pretreated at 873 K was extremely low, probably because of alloy formation.The results of XRD, XPS, and EXAFS demonstrate that the active species for methanol formation is a large metallic Cu particle covered with a partially oxidized layer interacting with highly dispersed ZnO.
View Morewebsite:http://www.angchenchem.com
Contact:+86-510-88302099 82327577
Address:Rm. 404/405, Floor 4th, No. 983 FengXiang Road, Wuxi, China
Jinan Hongfangde Pharmatech Co.,Ltd
Contact:86-531-88870908
Address:F Bldg. West Unit North Area of Univ. Tech. Garden Xinyu Rd. Jinan New & High Tech Industry Development Zone Shandong, China
Contact:21-7631221 15884421033
Address:326 Science and technology,Shanghai,China
HEZE KINGVOLT CHEMICAL CO., LTD
Contact:86-573-82118911
Address:Juancheng Industry Park
Contact:86-21-34622192,13917187091,21-34622765
Address:No. 500 Caobao Road Shanghai P.R China
Doi:10.1021/jo970892u
(1997)Doi:10.1039/c5ob00889a
(2015)Doi:10.1021/ja01930a004
(1910)Doi:10.1016/j.jorganchem.2006.10.053
(2007)Doi:10.1016/j.physc.2011.05.005
(2011)Doi:10.1039/a905161i
(1999)