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Ethylene glycol dry reforming on Ni/Al2O3 catalyst for syngas generation
被引:2
|作者:
Bahari, M. B.
[1
]
Jun, L. N.
[1
]
Shafiqah, M-N N.
[1
]
Fayaz, F.
[1
]
Vo, D-V N.
[1
,2
]
机构:
[1] Univ Malaysia Pahang, Fac Chem & Nat Resources Engn, Lebuhraya Tun Razak, Kuantan 26300, Pahang, Malaysia
[2] Univ Malaysia Pahang, Ctr Excellence Adv Res Fluid Flow, Kuantan 26300, Pahang, Malaysia
来源:
2018 3RD INTERNATIONAL CONFERENCE ON ENERGY MATERIALS AND APPLICATIONS
|
2018年
/
446卷
关键词:
HYDROGEN-PRODUCTION;
METHANE;
NI;
D O I:
10.1088/1757-899X/446/1/012013
中图分类号:
TE [石油、天然气工业];
TK [能源与动力工程];
学科分类号:
0807 ;
0820 ;
摘要:
It is the first time ethylene glycol dry reforming (EGDR) reaction was carried out for syngas production on 10%Ni/Al2O3 catalyst in a tubular fixed-bed reactor at atmospheric condition. Wet-impregnation method was employed for the synthesis of 10%Ni/Al2O3 catalyst. The results of X-ray diffraction measurement revealed the presence of gamma-Al2O3, NiO, NiAl2O4, Ni-0 and graphitic carbon phases on the surface of spent 10%Ni/Al2O3 catalyst. H-2 temperature-programmed reduction indicates that NiO and NiAl2O4 phases were totally reduced to metallic nickel phase at reduction temperature above 970 K. EGDR activity appeared to be steady with time-on-stream beyond 5-7 h. Catalytic activity was considerably improved with increasing feed ratio of CO2:C2H6O2 from 1:1 to 2.5:1.
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页数:6
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