| نویسندگان | فرشته مشکانی-مهران رضائی |
| نشریه | RSC ADV |
| تاریخ انتشار | 2015-5-01 |
| نمایه نشریه | ISI ,SCOPUS |
چکیده مقاله
The water gas shift reaction is one of the oldest heterogeneous catalytic reactions operating in industry for
H2 production with high purity and CO removal from syngas. Typical industrial catalyst for high temperature
water gas shift (HTS) reactions is Fe–Cr–Cu, but has environmental and safety concerns related to
chromium content, which has been regarded as a hazardous material. In this study, the effect of the
addition of alkali metal oxide promoters to chromium free Fe2O3–Al2O3–NiO catalyst was investigated in
HTS reaction. Nanocrystalline promoted chromium free catalysts with mesoporous structure were
synthesized by coprecipitation and impregnation methods. Brunner–Emmett–Teller (BET), X-ray
diffraction (XRD), temperature-programmed reduction (TPR) and desorption (TPD), scanning and
transmission electron microscopic (SEM, TEM) techniques were performed to elucidate the HTS catalytic
activity based on the influence of the addition of promoters on the catalyst structure. The results
indicated that the addition of alkali promoters was effective in suppressing methanation, as well as in
promoting HTS reaction activity for CO removal, which was related to the increment of the number of
weakly basic sites through the addition of promoter. The results revealed that the Fe2O3–Al2O3–NiO
(FAN) catalyst promoted by Na exhibited the highest catalytic activity and the lowest methanation among
the investigated catalysts under a low steam/gas molar ratio, which favored methane formation.
Furthermore, this catalyst presented higher CO removal activity than the commercial catalyst, which
contains chromium. Moreover, the effect of Na content on the structural and catalytic properties of the
FANNa catalysts was investigated and the results indicated that the catalyst with 3 wt% Na showed high
activity and stability during 50 h time on stream.