The role of ceria in promoting Ni catalysts supported on phosphate-modified zirconia for the partial oxidation of methane

被引:0
|
作者
Abahussain, Abdulaziz A. M. [1 ]
Al-Fatesh, Ahmed S. [1 ]
Vadodariya, Dharmesh M. [2 ]
Abu-Dahrieh, Jehad K. [3 ]
Banabdwin, Khaled M. [1 ]
Alarifi, Naif [4 ]
Ibrahim, Ahmed A. [1 ]
Fakeeha, Anis H. [1 ]
Abasaeed, Ahmed E. [1 ]
Kumar, Rawesh [2 ]
机构
[1] King Saud Univ, Coll Engn, Dept Chem Engn, POB 800, Riyadh 11421, Saudi Arabia
[2] Indus Univ, Dept Chem, Ahmadabad 382115, Gujarat, India
[3] Queens Univ Belfast, Sch Chem & Chem Engn, Belfast BT9 5AG, North Ireland
[4] King Abdulaziz City Sci & Technol KACST, Inst Refining & Petrochem Technol, Riyadh, Saudi Arabia
关键词
ceria promoter; cyclic H2TPR-O2TPO-H2TPR; Ni catalyst; partial oxidation of methane; phosphate-modified-zirconia; CALCIUM PHOSPHATE/HYDROXYAPATITE CATALYSTS; SYNGAS; IMPACT; STEAM;
D O I
10.1002/ese3.1820
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
The catalytic partial oxidation of methane (POM) is aimed at the mitigation of CH4 (a highly potent greenhouse gas) from the environment and the synthesis of syngas with a high H-2/CO ratio. Herein, to enhance the POM reaction, Ni-supported phosphate-modified-zirconia were synthesized with promotor "Ce" to achieve high H-2/CO ratio (2.4-3.2). The catalysts were characterized by surface area and porosity, X-ray diffraction, RAMAN, temperature-programmed experiments (TPR, CO2-TPD, and TPO), and TEM. Increasing the ceria addition over 10Ni/PO4 + ZrO2 resulted in lower crystallinity, higher dispersion of active sites, and enhanced the surface area of catalyst. The unique and prominent reducibility and basicity of NiO-species and surface oxide ions, respectively, are particularly notable at 4 wt.% ceria loading. At a reaction temperature of 600 degrees C, the highest concentration of active sites and a unique concentration of moderate strength basic sites can be achieved with 4 wt.% ceria loading over 10Ni/PO4 + ZrO2. This leads to 44% conversion of CH4, 36% yield of H-2, 35% yield of CO2, and H-2/CO ratio of 3.16 for the POM reaction. The cyclic H2TPR-O2TPO-H2TPR experiment confirms the reorganization of the active site towards high temperature under oxidizing gas O-2 and reducing gas H-2 gas stream during the POM reaction.
引用
收藏
页码:3379 / 3389
页数:11
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