甲醇
催化作用
选择性
化学
产量(工程)
空间速度
铜
无机化学
甲醇重整装置
化学工程
材料科学
有机化学
冶金
蒸汽重整
制氢
工程类
作者
Hironori Arakawa,Jean‐Luc Dubois,Kazuhiro Sayama
标识
DOI:10.1016/0196-8904(92)90051-w
摘要
As a chemical fixation and/or recycling technology of emitted CO2, a selective and effective conversion of CO2 to methanol by catalytic hydrogenation over promoted CuZnO catalyst has been studied. To obtain a high methanol selectivity, both a high pressure and a low temperature are required. The influence of contact time on the methanol selectivity was also demonstrated. It shows that methanol is directly produced from CO2 at low conversion as suggested by in situ FT-IR study, however, at high conversion, near the equilibrium, produced CO could also contribute to the methanol formation. The reduction temperature of catalyst influenced not only the catalyst structure but also the CO2 conversion and the methanol selectivity. Methanol yield was proportional to Cu metallic surface area of catalyst, and the CO2 hydrogenation to methanol over our catalysts was not a remarkable structure sensitive reaction. Finally, methanol was produced with 79 % selectivity, 20 % yield and 25 % CO2 conversion over CuOZnOAl2O3Cr2O3 catalyst at the condition of 7 MPa, 250 °C, GHSV=1800 h−1 and H2/CO2=3/1.
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