The promotional effect of K on the catalytic activity of Ni/MgAl2O4 for the combined H2O and CO2 reforming of coke oven gas for syngas production
A K-promoted 10Ni-(x)K/MgAl 2 O 4 catalyst was investigated for the combined H 2 O and CO 2 reforming (CSCR) of coke oven gas (COG) for syngas production. The 10Ni-(x)K/MgAl 2 O 4 catalyst was prepared by co-impregnation, and the K content was varied from 0 to 5 wt%. The BET, XRD, H 2 -chemisorption...
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Published in: | The Korean journal of chemical engineering Vol. 33; no. 11; pp. 3115 - 3120 |
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Main Authors: | , , , , |
Format: | Journal Article |
Language: | English |
Published: |
New York
Springer US
01-11-2016
Springer Nature B.V 한국화학공학회 |
Subjects: | |
Online Access: | Get full text |
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Summary: | A K-promoted 10Ni-(x)K/MgAl
2
O
4
catalyst was investigated for the combined H
2
O and CO
2
reforming (CSCR) of coke oven gas (COG) for syngas production. The 10Ni-(x)K/MgAl
2
O
4
catalyst was prepared by co-impregnation, and the K content was varied from 0 to 5 wt%. The BET, XRD, H
2
-chemisorption, H
2
-TPR, and CO
2
-TPD were performed for determining the physicochemical properties of prepared catalysts. Except under the condition of a K/Ni=0.1 (wt%/wt%), the Ni crystal size and dispersion decreased with increasing K/Ni. The coke resistance of the catalyst was investigated under conditions of CH
4
: CO
2
: H
2
: CO:N
2
=1 : 1 : 2 : 0.3 : 0.3, 800 °C, 5 atm. The coke formation on the used catalyst was examined by SEM and TG analysis. As compared to the 10Ni/MgAl
2
O
4
catalyst, the Kpromoted catalyst exhibited superior activity and coke resistance, attributed to its strong interaction with Ni and support, and the improved CO
2
adsorption characteristic. The 10Ni-1K/MgAl
2
O
4
catalyst exhibited optimum activity and coke resistance with only 1wt% of K. |
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Bibliography: | G704-000406.2016.33.11.020 |
ISSN: | 0256-1115 1975-7220 |
DOI: | 10.1007/s11814-016-0149-8 |