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.
引用
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页数:6
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